Catalyst systems for production of alpha olefin oligomers and polymers

ABSTRACT

Catalyst compositions containing N,N-bis[2-hydroxidebenzyl]amine transition metal compounds are disclosed. Methods for making these transition metal compounds and for using such compounds in catalyst compositions for the polymerization or oligomerization of alpha olefins also are provided.

REFERENCE TO RELATED APPLICATION

This application is a continuation application of U.S. patentapplication Ser. No. 13/338,362, filed on Dec. 28, 2011, now U.S. Pat.No. 8,791,217, the disclosure of which is incorporated herein byreference in its entirety.

BACKGROUND OF THE INVENTION

Mono-1-olefins (alpha olefins) can be polymerized with catalyst systemsemploying titanium, zirconium, vanadium, chromium, or other transitionmetals impregnated on a variety of support materials, often in thepresence of activators. There exists a need and a constant search todevelop new polymerization catalysts for alpha olefins, catalystactivation processes, and methods of making and using catalysts thatwill provide enhanced catalytic activities, selectivities, or newpolymeric materials tailored to specific end uses.

To that end, the present invention relates to amine bis(phenolate)transition metal compounds (e.g., N,N-bis[2-hydroxidebenzyl]aminetransition metal compounds) and catalyst compositions employing suchcompounds for the polymerization or oligomerization of alpha olefins.

SUMMARY OF THE INVENTION

This summary is provided to introduce a selection of concepts in asimplified form that are further described below in the detaileddescription. This summary is not intended to identify required oressential features of the claimed subject matter. Nor is this summaryintended to be used to limit the scope of the claimed subject matter.

The present invention generally relates to new catalyst compositions,methods for preparing catalyst compositions, methods for using thecatalyst compositions to polymerize/oligomerize alpha olefins, the alphaolefin oligomer products produced using such catalyst compositions, andarticles produced using these alpha olefin oligomer products. Inparticular, embodiments of the present invention are directed to aminebis(phenolate) or N,N-bis[2-hydroxidebenzyl]amine transition metalcompounds, and catalyst compositions employing such transition metalcompounds. Catalyst compositions of the present invention which containthese transition metal compounds can be used to produce, for example,alpha olefin polymer/oligomer products from monomers such as 1-hexene,1-octene, 1-decene, and the like.

In accordance with an embodiment of the present invention, disclosed anddescribed herein are transition metal compounds having the formula:

In formula (Ia), M can be Ti, Zr, or Hf, and X¹ and X² independently canbe a monoanionic ligand. Each R^(B) and R^(C) independently can be ahalide, a C₁ to C₃ hydrocarbyl group, a C₁ to C₃₆ halogenatedhydrocarbyl group, a C₁ to C₃₆ hydrocarboxy group, or a C₁ to C₃₆hydrocarbylsilyl group, wherein p and q independently can be 0, 1, 2, 3,or 4. R^(A) in formula (Ia) can be a C₁ to C₃₆ hydrocarbyl group or a C₁to C₃₆ halogenated hydrocarbyl group.

In accordance with another embodiment of the present invention,disclosed and described herein are transition metal compounds having theformula:

In formula (IIa), M can be Ti, Zr, or Hf, and X¹ and X² independentlycan be a monoanionic ligand. Each R^(B) and R^(C) independently can be ahalide, a C₁ to C₃₆ hydrocarbyl group, a C₁ to C₃₆ halogenatedhydrocarbyl group, a C₁ to C₃₆ hydrocarboxy group, or a C₁ to C₃₆hydrocarbylsilyl group, wherein p and q independently are 0, 1, 2, 3, or4. L in formula (IIa) can be a C₁ to C₁₈ hydrocarbylene group, while Dcan be a chemical group comprising at least one of nitrogen, oxygen,phosphorus, and sulfur.

In accordance with yet another embodiment of the present invention,disclosed and described herein are transition metal compounds having theformula:

In formula (IIIa), M can be Ti, Zr, or Hf, and X¹ and X² independentlycan be a monoanionic ligand. Each R^(B) and R^(C) independently can be ahalide, a C₁ to C₃₆ hydrocarbyl group, a C₁ to C₃₆ halogenatedhydrocarbyl group, a C₁ to C₃₆ hydrocarboxy group, or a C₁ to C₃₆hydrocarbylsilyl group, wherein p and q independently can be 0, 1, 2, 3,or 4. R^(B) in formula (IIIa) can be a C₂ to C₃₆ alkenyl group.

Catalyst compositions containing these transition metal complexes arealso provided by the present invention. In one embodiment, a catalystcomposition is disclosed which comprises an amine bis(phenolate) orN,N-bis[2-hydroxidebenzyl]amine transition metal complex and anactivator-support. Optionally, this catalyst composition can furthercomprise a co-catalyst. In some aspects, the co-catalyst can comprise anorganoaluminum compound, while in other aspects, the co-catalyst cancomprise an aluminoxane compound, an organoboron or organoboratecompound, an ionizing ionic compound, an organoaluminum compound, anorganozinc compound, an organomagnesium compound, an organolithiumcompound, or combinations thereof. More than one co-catalyst can bepresent in catalyst compositions disclosed herein.

The present invention also contemplates and encompasses alpha olefinpolymerization and oligomerization processes. Such processes cancomprise contacting a C₄ to C₆₀ alpha olefin and a catalyst compositionto produce an alpha olefin polymer/oligomer product. Generally, thecatalyst composition employed can comprise any of the transition metalcompounds disclosed herein and any of the activator-supports andoptional co-catalysts disclosed herein. For example, organoaluminumcompounds can be utilized in the catalyst compositions and/orpolymerization processes. Alpha olefin products produced by theseprocesses can be used to produce various articles of manufacture.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 presents the structures and abbreviations for compounds TM-1,TM-2, and TM-3 discussed herein.

FIG. 2 presents the structures and abbreviations for compounds TM-A,TM-B, TM-C, and TM-D discussed herein.

FIG. 3 presents a ¹H-NMR plot of TM-2 from Example 6.

FIG. 4 presents a plot of the molecular weight distributions of thealpha olefin polymer products of Examples 37-39.

DEFINITIONS

To define more clearly the terms used herein, the following definitionsare provided. Unless otherwise indicated, the following definitions areapplicable to this disclosure. If a term is used in this disclosure butis not specifically defined herein, the definition from the IUPACCompendium of Chemical Terminology, 2nd Ed (1997) can be applied, aslong as that definition does not conflict with any other disclosure ordefinition applied herein, or render indefinite or non-enabled any claimto which that definition is applied. To the extent that any definitionor usage provided by any document incorporated herein by referenceconflicts with the definition or usage provided herein, the definitionor usage provided herein controls.

Regarding claim transitional terms or phrases, the transitional term“comprising”, which is synonymous with “including,” “containing,” or“characterized by,” is inclusive or open-ended and does not excludeadditional, unrecited elements or method steps. The transitional phrase“consisting of” excludes any element, step, or ingredient not specifiedin the claim. The transitional phrase “consisting essentially of” limitsthe scope of a claim to the specified materials or steps and those thatdo not materially affect the basic and novel characteristic(s) of theclaimed invention. A “consisting essentially of” claim occupies a middleground between closed claims that are written in a “consisting of”format and fully open claims that are drafted in a “comprising” format.Absent an indication to the contrary, when describing a compound orcomposition “consisting essentially of” is not to be construed as“comprising,” but is intended to describe the recited component thatincludes materials which do not significantly alter composition ormethod to which the term is applied. For example, a feedstock consistingessentially of a material A can include impurities typically present ina commercially produced or commercially available sample of the recitedcompound or composition. When a claim includes different features and/orfeature classes (for example, a method step, feedstock features, and/orproduct features, among other possibilities), the transitional termscomprising, consisting essentially of, and consisting of, apply only tofeature class to which is utilized and it is possible to have differenttransitional terms or phrases utilized with different features within aclaim. For example a method can comprise several recited steps (andother non-recited steps) but utilize a catalyst system preparationconsisting of specific steps but utilize a catalyst system comprisingrecited components and other non-recited components. While compositionsand methods are described in terms of “comprising” various components orsteps, the compositions and methods can also “consist essentially of” or“consist of” the various components or steps, unless stated otherwise.For example, a catalyst composition consistent with embodiments of thepresent invention can comprise; alternatively, can consist essentiallyof; or alternatively, can consist of; (i) a transition metal compound,(ii) an activator-support, and (iii) optionally, a co-catalyst.

The terms “a,” “an,” “the,” etc., are intended to include pluralalternatives, e.g., at least one, unless otherwise specified. Forinstance, the disclosure of “an activator-support” or “a transitionmetal compound” is meant to encompass one, or mixtures or combinationsof more than one, activator-support or transition metal compound,respectively, unless otherwise specified.

Groups of elements of the table are indicated using the numbering schemeindicated in the version of the periodic table of elements published inChemical and Engineering News, 63(5), 27, 1985. In some instances, agroup of elements can be indicated using a common name assigned to thegroup; for example, alkali metals for Group 1 elements, alkaline earthmetals for Group 2 elements, transition metals for Group 3-12 elements,and halogens or halides for Group 17 elements.

For any particular compound disclosed herein, the general structure orname presented is also intended to encompass all structural isomers,conformational isomers, and stereoisomers that can arise from aparticular set of substituents, unless indicated otherwise. Thus, ageneral reference to a compound includes all structural isomers unlessexplicitly indicated otherwise; e.g., a general reference to pentaneincludes n-pentane, 2-methyl-butane, and 2,2-dimethylpropane, while ageneral reference to a butyl group includes an n-butyl group, asec-butyl group, an iso-butyl group, and a tert-butyl group.Additionally, the reference to a general structure or name encompassesall enantiomers, diastereomers, and other optical isomers whether inenantiomeric or racemic forms, as well as mixtures of stereoisomers, asthe context permits or requires. For any particular formula or name thatis presented, any general formula or name presented also encompasses allconformational isomers, regioisomers, and stereoisomers that can arisefrom a particular set of substituents.

A chemical “group” is described according to how that group is formallyderived from a reference or “parent” compound, for example, by thenumber of hydrogen atoms formally removed from the parent compound togenerate the group, even if that group is not literally synthesized inthis manner. These groups can be utilized as substituents or coordinatedor bonded to metal atoms. By way of example, an “alkyl group” formallycan be derived by removing one hydrogen atom from an alkane, while an“alkylene group” formally can be derived by removing two hydrogen atomsfrom an alkane. Moreover, a more general term can be used to encompass avariety of groups that formally are derived by removing any number (“oneor more”) hydrogen atoms from a parent compound, which in this examplecan be described as an “alkane group,” and which encompasses an “alkylgroup,” an “alkylene group,” and materials have three or more hydrogenatoms, as necessary for the situation, removed from the alkane.Throughout, the disclosure that a substituent, ligand, or other chemicalmoiety can constitute a particular “group” implies that the well-knownrules of chemical structure and bonding are followed when that group isemployed as described. When describing a group as being “derived by,”“derived from,” “formed by,” or “formed from,” such terms are used in aformal sense and are not intended to reflect any specific syntheticmethods or procedure, unless specified otherwise or the context requiresotherwise.

The term “substituted” when used to describe a group, for example, whenreferring to a substituted analog of a particular group, is intended todescribe any non-hydrogen moiety that formally replaces a hydrogen inthat group, and is intended to be non-limiting. A group or groups canalso be referred to herein as “unsubstituted” or by equivalent termssuch as “non-substituted,” which refers to the original group in which anon-hydrogen moiety does not replace a hydrogen within that group.Unless otherwise specified, “substituted” is intended to be non-limitingand include inorganic substituents or organic substituents as understoodby one of ordinary skill in the art.

The term “hydrocarbon” whenever used in this specification and claimsrefers to a compound containing only carbon and hydrogen. Otheridentifiers can be utilized to indicate the presence of particulargroups in the hydrocarbon (e.g. halogenated hydrocarbon indicates thatthe presence of one or more halogen atoms replacing an equivalent numberof hydrogen atoms in the hydrocarbon). The term “hydrocarbyl group” isused herein in accordance with the definition specified by IUPAC: aunivalent group formed by removing a hydrogen atom from a hydrocarbon(that is, a group containing only carbon and hydrogen). Non-limitingexamples of hydrocarbyl groups include ethyl, phenyl, tolyl, propenyl,and the like. Similarly, a “hydrocarbylene group” refers to a groupformed by removing two hydrogen atoms from a hydrocarbon, either twohydrogen atoms from one carbon atom or one hydrogen atom from each oftwo different carbon atoms. Therefore, in accordance with theterminology used herein, a “hydrocarbon group” refers to a generalizedgroup formed by removing one or more hydrogen atoms (as necessary forthe particular group) from a hydrocarbon. A “hydrocarbyl group,”“hydrocarbylene group,” and “hydrocarbon group” can be aliphatic oraromatic, acyclic or cyclic groups, and/or linear or branched. A“hydrocarbyl group,” “hydrocarbylene group,” and “hydrocarbon group” caninclude rings, ring systems, aromatic rings, and aromatic ring systems,which contain only carbon and hydrogen. “Hydrocarbyl groups,”“hydrocarbylene groups,” and “hydrocarbon groups” include, by way ofexample, aryl, arylene, arene groups, alkyl, alkylene, alkane group,cycloalkyl, cycloalkylene, cycloalkane groups, aralkyl, aralkylene, andaralkane groups, respectively, among other groups as members.

An aliphatic compound is a class of acyclic or cyclic, saturated orunsaturated, carbon compounds, excluding aromatic compounds. An“aliphatic group” is a generalized group formed by removing one or morehydrogen atoms (as necessary for the particular group) from carbon atomof an aliphatic compound. That is, an aliphatic compound is anon-aromatic organic compound. Aliphatic compounds and thereforealiphatic groups can contain organic functional group(s) and/or atom(s)other than carbon and hydrogen.

An aromatic compound is a compound containing a cyclically conjugateddouble bond system that follows the Hückel (4n+2) rule and contains(4n+2) pi-electrons, where n is an integer from 1 to 5. Aromaticcompounds include “arenes” (hydrocarbon aromatic compounds) and“heteroarenes,” also termed “hetarenes” (heteroaromatic compoundsformally derived from arenes by replacement of one or more methine (—C═)carbon atoms of the cyclically conjugated double bond system with atrivalent or divalent heteroatoms, in such a way as to maintain thecontinuous pi-electron system characteristic of an aromatic system and anumber of out-of-plane pi-electrons corresponding to the Hückel rule(4n+2). While arene compounds and heteroarene compounds are mutuallyexclusive members of the group of aromatic compounds, a compound thathas both an arene group and a heteroarene group are generally considereda heteroarene compound. Aromatic compounds, arenes, and heteroarenes canbe monocyclic (e.g., benzene, toluene, furan, pyridine, methylpyridine)or polycyclic unless otherwise specified. Polycyclic aromatic compounds,arenes, and heteroarenes, include, unless otherwise specified, compoundswherein the aromatic rings can be fused (e.g., naphthalene, benzofuran,and indole), compounds where the aromatic groups can be separate andjoined by a bond (e.g., biphenyl or 4-phenylpyridine), or compoundswhere the aromatic groups are joined by a group containing linking atoms(e.g., carbon—the methylene group in diphenylmethane; oxygen—diphenylether; nitrogen—triphenyl amine; among others linking groups). Asdisclosed herein, the term “substituted” can be used to describe anaromatic group, arene, or heteroarene wherein a non-hydrogen moietyformally replaces a hydrogen in the compound, and is intended to benon-limiting.

An “aromatic group” refers to a generalized group formed by removing oneor more hydrogen atoms (as necessary for the particular group and atleast one of which is an aromatic ring carbon atom) from an aromaticcompound. For a univalent “aromatic group,” the removed hydrogen atommust be from an aromatic ring carbon. For an “aromatic group” formed byremoving more than one hydrogen atom from an aromatic compound, at leastone hydrogen atom must be from an aromatic hydrocarbon ring carbon.Additionally, an “aromatic group” can have hydrogen atoms removed fromthe same ring of an aromatic ring or ring system (e.g., phen-1,4-ylene,pyridin-2,3-ylene, naphth-1,2-ylene, and benzofuran-2,3-ylene), hydrogenatoms removed from two different rings of a ring system (e.g.,naphth-1,8-ylene and benzofuran-2,7-ylene), or hydrogen atoms removedfrom two isolated aromatic rings or ring systems (e.g.,bis(phen-4-ylene)methane).

The term “alkane” whenever used in this specification and claims refersto a saturated hydrocarbon compound. Other identifiers can be utilizedto indicate the presence of particular groups in the alkane (e.g.halogenated alkane indicates that the presence of one or more halogenatoms replacing an equivalent number of hydrogen atoms in the alkane).The term “alkyl group” is used herein in accordance with the definitionspecified by IUPAC: a univalent group formed by removing a hydrogen atomfrom an alkane. Similarly, an “alkylene group” refers to a group formedby removing two hydrogen atoms from an alkane (either two hydrogen atomsfrom one carbon atom or one hydrogen atom from two different carbonatoms). An “alkane group” is a general term that refers to a groupformed by removing one or more hydrogen atoms (as necessary for theparticular group) from an alkane. An “alkyl group,” “alkylene group,”and “alkane group” can be acyclic or cyclic groups, and/or can be linearor branched unless otherwise specified. Primary, secondary, and tertiaryalkyl group are derived by removal of a hydrogen atom from a primary,secondary, tertiary carbon atom, respectively, of an alkane. The n-alkylgroup can be derived by removal of a hydrogen atom from a terminalcarbon atom of a linear alkane. The groups RCH₂ (R≠H), R₂CH (R≠H), andR₃C (R≠H) are primary, secondary, and tertiary alkyl groups,respectively.

A cycloalkane is a saturated cyclic hydrocarbon, with or without sidechains, for example, cyclobutane. Other identifiers can be utilized toindicate the presence of particular groups in the cycloalkane (e.g.halogenated cycloalkane indicates that the presence of one or morehalogen atoms replacing an equivalent number of hydrogen atoms in thecycloalkane). Unsaturated cyclic hydrocarbons having one endocyclicdouble or one triple bond are called cycloalkenes and cycloalkynes,respectively. Those having more than one such multiple bond arecycloalkadienes, cycloalkatrienes, and so forth. Other identifiers canbe utilized to indicate the presence of particular groups in thecycloalkene, cycloalkadienes, cycloalkatrienes, and so forth.

A “cycloalkyl group” is a univalent group derived by removing a hydrogenatom from a ring carbon atom from a cycloalkane. For example, a1-methylcyclopropyl group and a 2-methylcyclopropyl group areillustrated as follows.

Similarly, a “cycloalkylene group” refers to a group derived by removingtwo hydrogen atoms from a cycloalkane, at least one of which is a ringcarbon. Thus, a “cycloalkylene group” includes both a group derived froma cycloalkane in which two hydrogen atoms are formally removed from thesame ring carbon, a group derived from a cycloalkane in which twohydrogen atoms are formally removed from two different ring carbons, anda group derived from a cycloalkane in which a first hydrogen atom isformally removed from a ring carbon and a second hydrogen atom isformally removed from a carbon atom that is not a ring carbon. An“cycloalkane group” refers to a generalized group formed by removing oneor more hydrogen atoms (as necessary for the particular group and atleast one of which is a ring carbon) from a cycloalkane.

The term “alkene” whenever used in this specification and claims refersa linear or branched hydrocarbon olefin that has one carbon-carbondouble bond and the general formula C_(n)H_(2n). Alkadienes refer to alinear or branched hydrocarbon olefin having two carbon-carbon doublebonds and the general formula C_(n)H_(2n-2) and alkatrienes refer tolinear or branched hydrocarbon olefins having three carbon-carbon andthe general formula C_(n)H_(2n-4). Alkenes, alkadienes, and alkatrienescan be further identified by the position of the carbon-carbon doublebond(s). Other identifiers can be utilized to indicate the presence orabsence of particular groups within an alkene, alkadiene, or alkatriene.For example, a haloalkene refers to an alkene having one or morehydrogen atoms replace with a halogen atom.

An “alkenyl group” is a univalent group derived from an alkene byremoval of a hydrogen atom from any carbon atom of the alkene. Thus,“alkenyl group” includes groups in which the hydrogen atom is formallyremoved from an sp² hybridized (olefinic) carbon atom and groups inwhich the hydrogen atom is formally removed from any other carbon atom.For example and unless otherwise specified, 1-propenyl (—CH═CHCH₃),2-propenyl [(CH₃)C═CH₂], and 3-propenyl (—CH₂CH═CH₂) groups areencompassed with the term “alkenyl group.” Similarly, an “alkenylenegroup” refers to a group formed by formally removing two hydrogen atomsfrom an alkene, either two hydrogen atoms from one carbon atom or onehydrogen atom from two different carbon atoms. An “alkene group” refersto a generalized group formed by removing one or more hydrogen atoms (asnecessary for the particular group) from an alkene. When the hydrogenatom is removed from a carbon atom participating in a carbon-carbondouble bond, the regiochemistry of the carbon from which the hydrogenatom is removed, and regiochemistry of the carbon-carbon double bond canboth be specified. Other identifiers can be utilized to indicate thepresence or absence of particular groups within an alkene group. Alkenegroups can also be further identified by the position of thecarbon-carbon double bond.

The term “alkyne” whenever used in this specification and claims refersto a linear or branched hydrocarbon olefin that has one carbon-carbontriple bond and the general formula C_(n)H_(2n-2). Alkadiynes refer to ahydrocarbon olefin having two carbon-carbon double bonds and the generalformula C_(n)H_(2n-6) and alkatriynes refer to hydrocarbon olefinshaving three carbon-carbon and the general formula C_(n)H_(2n-10).Alkynes, alkadiynes, and alkatriynes can be further identified by theposition of the carbon-carbon triple bond(s). Other identifiers can beutilized to indicate the presence or absence of particular groups withinan alkene, alkadiene, or alkatriene. For example, a haloalkyne refers toan alkyne having one or more hydrogen atoms replace with a halogen atom.

An “alkynyl group” is a univalent group derived from an alkyne byremoval of a hydrogen atom from any carbon atom of the alkyne. Thus,“alkynyl group” includes groups in which the hydrogen atom is formallyremoved from an sp hybridized (acetylenic) carbon atom and groups inwhich the hydrogen atom is formally removed from any other carbon atom.For example and unless otherwise specified, 1-propynyl(—C≡CCH₃) and3-propynyl(HC≡CCH₂—) groups are all encompassed with the term “alkynylgroup.” Similarly, an “alkynylene group” refers to a group formed byformally removing two hydrogen atoms from an alkyne, either two hydrogenatoms from one carbon atom if possible or one hydrogen atom from twodifferent carbon atoms. An “alkyne group” refers to a generalized groupformed by removing one or more hydrogen atoms (as necessary for theparticular group) from an alkyne. Other identifiers can be utilized toindicate the presence or absence of particular groups within an alkynegroup. Alkyne groups can also be further identified by the position ofthe carbon-carbon triple bond.

The term “olefin” whenever used in this specification and claims refersto compound that has at least one carbon-carbon double bond that is notpart of an aromatic ring or ring system. The term “olefin” includesaliphatic, aromatic, cyclic or acyclic, and/or linear and branchedcompounds having at least one carbon-carbon double bond that is not partof an aromatic ring or ring system unless specifically stated otherwise.The term “olefin,” by itself, does not indicate the presence or absenceof heteroatoms and/or the presence or absence of other carbon-carbondouble bonds unless explicitly indicated. Olefins can also be furtheridentified by the position of the carbon-carbon double bond. It is notedthat alkenes, alkadienes, alkatrienes, cycloalkenes, cycloalkadienes,are members of the class of olefins. The olefin can be furtheridentified by the position of the carbon-carbon double bond(s).

The term “alpha olefin” as used in this specification and claims refersto an olefin that has a double bond between the first and second carbonatom of a contiguous chain of carbon atoms. The term “alpha olefin”includes linear and branched alpha olefins unless expressly statedotherwise. In the case of branched alpha olefins, a branch can be at the2-position (a vinylidene) and/or the 3-position or higher with respectto the olefin double bond. The term “vinylidene” whenever used in thisspecification and claims refers to an alpha olefin having a branch atthe 2-position with respect to the olefin double bond. By itself, theterm “alpha olefin” does not indicate the presence or absence ofheteroatoms and/or the presence or absence of other carbon-carbon doublebonds unless explicitly indicated. The terms “hydrocarbon alpha olefin”or “alpha olefin hydrocarbon” refer to alpha olefin compounds containingonly hydrogen and carbon.

The term “linear alpha olefin” as used herein refers to a linear olefinhaving a double bond between the first and second carbon atom. The term“linear alpha olefin” by itself does not indicate the presence orabsence of heteroatoms and/or the presence or absence of othercarbon-carbon double bonds, unless explicitly indicated. The terms“linear hydrocarbon alpha olefin” or “linear alpha olefin hydrocarbon”refers to linear alpha olefin compounds containing only hydrogen andcarbon.

The term “normal alpha olefin” whenever used in this specification andclaims refers to a linear hydrocarbon mono-olefin having a double bondbetween the first and second carbon atom. It is noted that “normal alphaolefin” is not synonymous with “linear alpha olefin” as the term “linearalpha olefin” can include linear olefinic compounds having a double bondbetween the first and second carbon atoms and having heteroatoms and/oradditional double bonds.

A “heterocyclic compound” is a cyclic compound having at least twodifferent elements as ring member atoms. For example, heterocycliccompounds can comprise rings containing carbon and nitrogen (forexample, tetrahydropyrrole), carbon and oxygen (for example,tetrahydrofuran), or carbon and sulfur (for example,tetrahydrothiophene), among others. Heterocyclic compounds andheterocyclic groups can be either aliphatic or aromatic.

A “heterocyclyl group” is a univalent group formed by removing ahydrogen atom from a heterocyclic ring or ring system carbon atom of aheterocyclic compound. By specifying that the hydrogen atom is removedfrom a heterocyclic ring or ring system carbon atom, a “heterocyclylgroup” is distinguished from a “cycloheteryl group,” in which a hydrogenatom is removed from a heterocyclic ring or ring system heteroatom. Forexample, a pyrrolidin-2-yl group illustrated below is one example of a“heterocyclyl group,” and a pyrrolidin-1-yl group illustrated below isone example of a “cycloheteryl” group.”

Similarly, a “heterocyclylene group” or more simply, a “heterocyclenegroup,” refers to a group formed by removing two hydrogen atoms from aheterocyclic compound, at least one of which is from a heterocyclic ringor ring system carbon. Thus, in a “heterocyclylene group,” at least onehydrogen is removed from a heterocyclic ring or ring system carbon atom,and the other hydrogen atom can be removed from any other carbon atom,including for example, the same heterocyclic ring or ring system carbonatom, a different heterocyclic ring or ring system ring carbon atom, ora non-ring carbon atom. A “heterocyclic group” refers to a generalizedgroup formed by removing one or more hydrogen atoms (as necessary forthe particular group and at least one of which is a heterocyclic ringcarbon atom) from a heterocyclic compound. Generally, a heterocycliccompound can be aliphatic or aromatic unless otherwise specified.

A “cycloheteryl group” is a univalent group formed by removing ahydrogen atom from a heterocyclic ring or ring system heteroatom of aheterocyclic compound, as illustrated. By specifying that the hydrogenatom is removed from a heterocyclic ring or ring system heteroatom andnot from a ring carbon atom, a “cycloheteryl group” is distinguishedfrom a “heterocyclyl group” in which a hydrogen atom is removed from aheterocyclic ring or ring system carbon atom. Similarly, a“cycloheterylene group” refers to a group formed by removing twohydrogen atoms from an heterocyclic compound, at least one of which isremoved from a heterocyclic ring or ring system heteroatom of theheterocyclic compound; the other hydrogen atom can be removed from anyother atom, including for example, a heterocyclic ring or ring systemring carbon atom, another heterocyclic ring or ring system heteroatom,or a non-ring atom (carbon or heteroatom). A “cyclohetero group” refersto a generalized group formed by removing one or more hydrogen atoms (asnecessary for the particular group and at least one of which is from aheterocyclic ring or ring system heteroatom) from a heterocycliccompound.

An arene is aromatic hydrocarbon, with or without side chains (e.g.benzene, toluene, or xylene, among others. An “aryl group” is a groupderived from the formal removal of a hydrogen atom from an aromatic ringcarbon of an arene. It should be noted that the arene can contain asingle aromatic hydrocarbon ring (e.g., benzene, or toluene), containfused aromatic rings (e.g., naphthalene or anthracene), and contain oneor more isolated aromatic rings covalently linked via a bond (e.g.,biphenyl) or non-aromatic hydrocarbon group(s) (e.g., diphenylmethane).One example of an “aryl group” is ortho-tolyl (o-tolyl), the structureof which is shown here.

Similarly, an “arylene group” refers to a group formed by removing twohydrogen atoms (at least one of which is from an aromatic ring carbon)from an arene. An “arene group” refers to a generalized group formed byremoving one or more hydrogen atoms (as necessary for the particulargroup and at least one of which is an aromatic ring carbon) from anarene. However, if a group contains separate and distinct arene andheteroarene rings or ring systems (e.g. the phenyl and benzofuranmoieties in 7-phenylbenzofuran) its classification depends upon theparticular ring or ring system from which the hydrogen atom was removed,that is, an arene group if the removed hydrogen came from the aromatichydrocarbon ring or ring system carbon atom (e.g. the 2 carbon atom inthe phenyl group of 6-phenylbenzofuran and a heteroarene group if theremoved hydrogen carbon came from a heteroaromatic ring or ring systemcarbon atom (e.g. the 2 or 7 carbon atom of the benzofuran group or6-phenylbenzofuran). It should be noted that according the definitionsprovided herein, general arene groups (including an aryl group and anareylene group) include those having zero, one, or more than onehydrocarbyl substituent groups located on an aromatic hydrocarbon ringor ring system carbon atom (e.g., a toluene group or a xylene group,among others) and is a member of the group of hydrocarbon groups.However, a phenyl group (or phenylene group) and/or a naphthyl group (ornaphthylene group) refer to the specific unsubstituted arene groups(including no hydrocarbyl group located on an aromatic hydrocarbon ringor ring system carbon atom). Consequently, a substituted phenyl group orsubstituted naphthyl group refers to the respective arene group havingone or more substituent groups (including halogens, hydrocarbyl groups,or hydrocarboxy groups, among others) located on an aromatic hydrocarbonring or ring system carbon atom. When the substituted phenyl groupand/or substituted naphthyl group is a member of the group ofhydrocarbon groups (or a member of the general group of arene groups),each substituent is limited to a hydrocarbyl substituent group. Onehaving ordinary skill in the art can readily discern and select generalphenyl and/or naphthyl groups, specific phenyl and/or naphthyl groups,and/or individual substituted phenyl or substituted naphthyl groupswhich can be utilized as a member of the group of hydrocarbon groups (ora member of the general group of arene groups).

A heteroarene is aromatic compound, with or without side chains, havinga heteroatom within the aromatic ring or aromatic ring system (e.g.pyridine, indole, or benzofuran, among others). A “heteroaryl group” isa class of “heterocyclyl group” and is a univalent group formed byremoving a hydrogen atom from a heteroaromatic ring or ring systemcarbon atom of a heteroarene compound. By specifying that the hydrogenatom is removed from a ring carbon atom, a “heteroaryl group” isdistinguished from an “arylheteryl group,” in which a hydrogen atom isremoved from a heteroaromatic ring or ring system heteroatom. Forexample, an indol-2-yl group illustrated below is one example of a“heteroaryl group,” and an indol-1-yl group illustrated below is oneexample of an “arylheteryl” group.”

Similarly, a “heteroarylene group” refers to a group formed by removingtwo hydrogen atoms from a heteroarene compound, at least one of which isfrom a heteroarene ring or ring system carbon atom. Thus, in a“heteroarylene group,” at least one hydrogen is removed from aheteroarene ring or ring system carbon atom, and the other hydrogen atomcan be removed from any other carbon atom, including for example, aheteroarene ring or ring system carbon atom, or a non-heteroarene ringor ring system atom. A “heteroarene group” refers to a generalized groupformed by removing one or more hydrogen atoms (as necessary for theparticular group and at least one of which is a heteroarene ring or ringsystem carbon atom) from a heteroarene compound. If a hydrogen atom isremoved from a heteroaromatic ring or ring system heteroatom and from aheteroaromatic ring or ring system carbon atom or an aromatichydrocarbon ring or ring system carbon atom, the group is classified asan “arylheterylene group” or an “arylhetero group.”

An “arylheteryl group” is a class of “cycloheteryl group” and is aunivalent group formed by removing a hydrogen atom from a heteroaromaticring or ring system heteroatom, as illustrated. By specifying that thehydrogen atom is removed from of a heteroaromatic ring or ring systemheteroatom and not from a heteroaromatic ring or ring system carbonatom, an “arylheteryl group” is distinguished from a “heteroaryl group”in which a hydrogen atom is removed from a heteroaromatic ring or a ringsystem carbon atom. Similarly, an “arylheterylene group” refers to agroup formed by removing two hydrogen atoms from a heteroaryl compound,at least one of which is removed from a heteroaromatic ring or ringsystem heteroatom of the heteroaryl compound, the other hydrogen atomcan be removed from any other atom, including for example, aheteroaromatic ring or ring system carbon atom, another heteroaromaticring or ring system heteroatom, or a non-ring atom (carbon orheteroatom) from a heteroaromatic compound. An “arylhetero group” refersto a generalized group formed by removing one or more hydrogen atoms (asnecessary for the particular group and at least one of which is from aheteroaromatic ring or ring system) heteroatom from a heteroarenecompound.

An “aralkyl group” is an aryl-substituted alkyl group having a freevalance at a non-aromatic carbon atom (e.g. a benzyl group, or a2-phenyleth-lyl group, among others). Similarly, an “aralkylene group”is an aryl-substituted alkylene group having two free valences at asingle non-aromatic carbon atom or a free valence at two non-aromaticcarbon atoms while an “aralkane group” is a generalized is anaryl-substituted alkane group having one or more free valences at anon-aromatic carbon atom(s). A “heteroaralkyl group” is aheteroaryl-substituted alkyl group having a free valence at anon-heteroaromatic ring or ring system carbon atom. Similarly a“heteroaralkylene group” is a heteroaryl-substituted alkylene grouphaving two free valences at a single non-heteroaromatic ring or ringsystem carbon atom or a free valence at two non-heteroaromatic ring orring system carbon atoms while a “heteroaralkane group” is a generalizedaryl-substituted alkane group having one or more free valences at anon-heteroaromatic ring or ring system carbon atom(s). It should benoted that according the definitions provided herein, general aralkanegroups include those having zero, one, or more than one hydrocarbylsubstituent groups located on an aralkane aromatic hydrocarbon ring orring system carbon atom and is a member of the group of hydrocarbongroups. However, specific aralkane groups specifying a particular arylgroup (e.g. the phenyl group in a benzyl group or a 2-phenylethyl group,among others) refer to the specific unsubstituted aralkane groups(including no hydrocarbyl group located on the aralkane aromatichydrocarbon ring or ring system carbon atom). Consequently, asubstituted aralkane group specifying a particular aryl group refers toa respective aralkane group having one or more substituent groups(including halogens, hydrocarbyl groups, or hydrocarboxy groups, amongothers). When the substituted aralkane group specifying a particulararyl group is a member of the group of hydrocarbon groups (or a memberof the general group of aralkane groups), each substituent is limited toa hydrocarbyl substituent group. One can readily discern and selectsubstituted aralkane groups specifying a particular aryl group which canbe utilized as a member of the group of hydrocarbon groups (or a memberof the general group of aralkane groups).

A “halide” has its usual meaning. Examples of halides include fluoride,chloride, bromide, and iodide.

The terms “product,” “alpha olefin product,” “polymer product,”“polymerization product,” “polymer,” “oligomer product,”“oligomerization product,” “oligomer,” “alpha olefin oligomer,” and thelike, are used generically and interchangeably to encompass any of theproducts, excluding monomer(s), regardless of molecular weight, producedby the contacting of an alpha olefin monomer with a catalyst composition(e.g., an oligomerization reaction, a polymerization reaction, etc.),and the alpha olefin products disclosed herein can range inweight-average molecular weight (M_(w)) from about 1,000 g/mol to over1,000,000 g/mol. Moreover, these terms are also used generically hereinto include alpha olefin homopolymers, copolymers, terpolymers, and soforth. A copolymer is derived from an alpha olefin monomer and one alphaolefin comonomer, while a terpolymer is derived from an alpha olefinmonomer and two alpha olefin comonomers. Accordingly, “polymer” and“oligomer” encompass copolymers, terpolymers, etc., derived from anyalpha olefin monomer and comonomer(s) disclosed herein.

In like manner, the scope of the term “polymerization” (or“oligomerization”) includes homopolymerization, copolymerization,terpolymerization, etc. Therefore, a copolymerization process wouldinvolve contacting one alpha olefin monomer and one alpha olefincomonomer to produce a copolymer.

The alpha olefin product in combination with residual monomer frompreparing the product and any other material which exits the reactor istermed the “polymerization reactor effluent,” “oligomerization reactoreffluent,” “reactor effluent,” or similar terms.

A “heavy oligomer product” is the product that results from removingsome of the lower alpha olefin oligomers from the alpha olefin productwithin the reactor effluent. In an aspect, the process utilized toremove some of the lower alpha olefin oligomers can be distillation. Inanother aspect, the process utilized to remove some of the lower alphaolefin oligomers can be purging or sparging. In yet another aspect, theprocess to remove some of the lower alpha olefin oligomers can bedistillation using a gas purge. When the material being distilled,purged, or sparged also contains some alpha olefin monomer (e.g.,reactor effluent wherein not all of the alpha olefin monomer isconverted to an alpha olefin polymerization or oligomerization product),the distillation, purging, or sparging can also remove some or all ofthe alpha olefin monomer. Consequently, depending upon thepolymerization method and the fractionation method, the heavy oligomerproduct can contain less than some specified amount of alpha olefinmonomer (e.g., less than 1 weight percent based on the total weight ofthe heavy oligomer product). Generally, the process of removing some ofthe lower alpha olefin oligomers removes at least a portion of the alphaolefin monomer, the dimer, and/or the trimer to form the heavy oligomerproduct. It is noted that when the method utilized to remove some of thelower alpha olefin oligomers, by its nature, the method can also removea portion of the higher olefin oligomers, and this point does notdetract from the intent to remove a portion of the lower alpha olefinoligomers. In some cases, the term alpha olefin product can be used todescribe the reaction product both before and after distillation, inwhich case, reference to the context and experimental details can bemade to determine whether the product has been distilled or not.

A “polyalphaolefin” (PAO) is a mixture of hydrogenated (oralternatively, substantially saturated) oligomers, containing unitsderived from an alpha olefin monomer. Unless specified otherwise, thePAO can contain units derived from alpha olefin monomer units, which canbe the same (hydrogenated or substantially saturated alpha olefinhomooligomer) or can be different (hydrogenated or substantiallysaturated alpha olefin co-oligomer). One having ordinary skill in theart will recognize that depending on the process utilized to produce thePAO, the as-produced alpha olefin oligomers can already be substantiallysaturated. For example, a process which is carried out in the presenceof hydrogen can produce an olefin oligomer which may or may not requirea separate hydrogenation step to provide a product with the desiredproperties. Generally, the alpha olefin monomer utilized to produce thepolyalphaolefin can be any alpha olefin monomer described herein. Onehaving ordinary skill in the art would recognize that the process(es)for producing the PAO can leave some hydrogenated monomer in the PAO(e.g., less than 1 weight % based on the total amount of the PAO), andthis quantity of hydrogenated monomer can be specified.

The term “consists essentially of normal alpha olefin(s)” or variationsthereof are used in the specification and claims to refer tocommercially available normal alpha olefin monomer(s). The commerciallyavailable normal alpha olefin can contain non-normal alpha olefinimpurities such as vinylidenes, internal olefins, branched alphaolefins, paraffins, and diolefins, among other impurities, which are notremoved during the normal alpha olefin production process. One ofordinary skill in the art will recognize that the identity and quantityof the specific impurities present in the commercial normal alpha olefinwill depend upon the source of commercial normal alpha olefin.Additionally, when applied to a normal alpha olefin of a single carbonnumber, the term “consists essentially of a normal alpha olefin(s)” alsoincludes small quantities (e.g., less than 5, 4, 3, 2, or 1 weight %) ofolefins having a different carbon number than the recited normal alphaolefin carbon number which are not removed during the single carbonnumber normal alpha olefin production process. Consequently, the term“consists essentially of normal alpha olefins” and its variants are notintended to limit the amount/quantity of the non-linear alpha olefincomponents (or in relation to carbon number the amount of a non-recitedcarbon number) any more stringently than the amounts/quantities presentin a particular commercial normal alpha olefin, unless explicitlystated. One source of commercially available alpha olefin monomer isthose produced by the oligomerization of ethylene. A second source ofcommercially available alpha olefin monomer is those which are produced,and optionally isolated from, Fischer-Tropsch synthesis streams. Onesource of commercially available normal alpha olefin monomers producedby ethylene oligomerization which can be utilized as an olefin feedstockis Chevron Phillips Chemical Company LP, The Woodlands, Tex., USA. Othersources of commercially available normal alpha olefin monomers producedby ethylene oligomerization which can be utilized as an olefin feedstockinclude Ineos Oligomers (Feluy, Belgium), Shell Chemicals Corporation(Houston, Tex., USA or London. United Kingdom), Idemitsu Kosan (Tokyo,Japan), and Mitsubishi Chemical Corporation (Tokyo, Japan), amongothers. One source of commercially available normal alpha olefinmonomers produced, and optionally isolated from Fisher-Tropsch synthesisstreams includes Sasol (Johannesburg, South Africa), among others.

The term “co-catalyst” is used generally herein to refer to compoundssuch as aluminoxane compounds, organoboron or organoborate compounds,ionizing ionic compounds, organoaluminum compounds, organozinccompounds, organomagnesium compounds, organolithium compounds, and thelike, that can constitute one component of a catalyst composition, whenused in addition to an activator-support. The term “co-catalyst” is usedregardless of the actual function of the compound or any chemicalmechanism by which the compound may operate.

The terms “chemically-treated solid oxide,” “treated solid oxidecompound,” and the like, are used herein to indicate a solid, inorganicoxide of relatively high porosity, which can exhibit Lewis acidic orBrønsted acidic behavior, and which has been treated with anelectron-withdrawing component, typically an anion, and which iscalcined. The electron-withdrawing component is typically anelectron-withdrawing anion source compound. Thus, the chemically-treatedsolid oxide can comprise a calcined contact product of at least onesolid oxide with at least one electron-withdrawing anion sourcecompound. Typically, the chemically-treated solid oxide comprises atleast one acidic solid oxide compound. The “activator-support” of thepresent invention can be a chemically-treated solid oxide. The terms“support” and “activator-support” are not used to imply these componentsare inert, and such components should not be construed as an inertcomponent of the catalyst composition. The term “activator,” as usedherein, refers generally to a substance that is capable of converting atransition metal component into a catalyst that can polymerize alphaolefins, or converting a contact product of a transition metal compoundand a component that provides an activatable ligand (e.g., an alkyl, ahydride) to the transition metal compound, when the transition metalcompound does not already comprise such a ligand, into a catalyst thatcan polymerize alpha olefins. This term is used regardless of the actualactivating mechanism. If the catalyst composition contains anactivator-support, then aluminoxanes, organoboron or organoboratecompounds, ionizing ionic compounds, and the like, are typicallyreferred to as co-catalysts.

The term “fluoroorgano boron compound” is used herein with its ordinarymeaning to refer to neutral compounds of the form BY₃. The term“fluoroorgano borate compound” also has its usual meaning to refer tothe monoanionic salts of a fluoroorgano boron compound of the form[cation]⁺[BY₄]⁻, where Y represents a fluorinated organic group.Materials of these types are generally and collectively referred to as“organoboron or organoborate compounds.”

Compounds having formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb)can be described herein as amine bis(phenolate) complexes or compounds,N,N-bis[2-hydroxidebenzyl]amine complexes or compounds,bis[2-hydroxidebenzyl]amine complexes or compounds, or simply transitionmetal complexes or compounds, and such terminology will be usedinterchangeably throughout this disclosure to describe compounds havingformulas (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb).

The terms “catalyst composition,” “catalyst mixture,” “catalyst system,”and the like, do not depend upon the actual product or compositionresulting from the contact or reaction of the initial components of theclaimed catalyst composition/mixture/system, the nature of the activecatalytic site, or the fate of the co-catalyst, the transition metalcompound(s), any olefin monomer used to prepare a precontacted mixture,or the activator (e.g., activator-support), after combining thesecomponents. Therefore, the terms “catalyst composition,” “catalystmixture,” “catalyst system,” and the like, encompass the initialstarting components of the composition, as well as whatever product(s)may result from contacting these initial starting components, and thisis inclusive of both heterogeneous and homogenous catalyst systems orcompositions. The terms “catalyst composition,” “catalyst mixture,”“catalyst system,” and the like, will be used interchangeably throughoutthis disclosure.

The term “contact product” is used herein to describe compositionswherein the components are contacted together in any order, in anymanner, and for any length of time. For example, the components can becontacted by blending or mixing. Further, contacting of any componentcan occur in the presence or absence of any other component of thecompositions described herein. Combining additional materials orcomponents can be done by any suitable method. Further, the term“contact product” includes mixtures, blends, solutions, slurries,reaction products, and the like, or combinations thereof. Although“contact product” can include reaction products, it is not required forthe respective components to react with one another. Similarly, the term“contacting” is used herein to refer to materials which can be blended,mixed, slurried, dissolved, reacted, treated, or otherwise contacted insome other manner.

The term “precontacted” mixture is used herein to describe a firstmixture of catalyst components that are contacted for a first period oftime prior to the first mixture being used to form a “postcontacted” orsecond mixture of catalyst components that are contacted for a secondperiod of time. Typically, the precontacted mixture can describe amixture of transition metal compound (one or more than one), olefinmonomer (or monomers), and organoaluminum compound (or compounds),before this mixture is contacted with an activator-support(s) andoptional additional organoaluminum compound. Thus, precontacteddescribes components that are used to contact each other, but prior tocontacting the components in the second, postcontacted mixture.Accordingly, this invention can occasionally distinguish between acomponent used to prepare the precontacted mixture and that componentafter the mixture has been prepared. For example, according to thisdescription, it is possible for the precontacted organoaluminumcompound, once it is contacted with the transition metal compound andthe olefin monomer, to have reacted to form at least one differentchemical compound, formulation, or structure from the distinctorganoaluminum compound used to prepare the precontacted mixture. Inthis case, the precontacted organoaluminum compound or component isdescribed as comprising an organoaluminum compound that was used toprepare the precontacted mixture.

Additionally, the precontacted mixture can describe a mixture oftransition metal compound(s) and organoaluminum compound(s), prior tocontacting this mixture with an activator-support(s). This precontactedmixture also can describe a mixture of transition metal compound(s),olefin monomer(s), and activator-support(s), before this mixture iscontacted with an organoaluminum co-catalyst compound or compounds.

Similarly, the term “postcontacted” mixture is used herein to describe asecond mixture of catalyst components that are contacted for a secondperiod of time, and one constituent of which is the “precontacted” orfirst mixture of catalyst components that were contacted for a firstperiod of time. Typically, the term “postcontacted” mixture is usedherein to describe the mixture of transition metal compound(s), olefinmonomer(s), organoaluminum compound(s), and activator-support(s) formedfrom contacting the precontacted mixture of a portion of thesecomponents with any additional components added to make up thepostcontacted mixture. Often, the activator-support can comprise achemically-treated solid oxide. For instance, the additional componentadded to make up the postcontacted mixture can be a chemically-treatedsolid oxide (one or more than one), and optionally, can include anorganoaluminum compound which is the same as or different from theorganoaluminum compound used to prepare the precontacted mixture, asdescribed herein. Accordingly, this invention can also occasionallydistinguish between a component used to prepare the postcontactedmixture and that component after the mixture has been prepared.

Although any methods, devices, and materials similar or equivalent tothose described herein can be used in the practice or testing of theinvention, the typical methods, devices and materials are hereindescribed.

All publications and patents mentioned herein are incorporated herein byreference for the purpose of describing and disclosing, for example, theconstructs and methodologies that are described in the publications,which might be used in connection with the presently describedinvention. The publications discussed throughout the text are providedsolely for their disclosure prior to the filing date of the presentapplication. Nothing herein is to be construed as an admission that theinventors are not entitled to antedate such disclosure by virtue ofprior invention.

Applicants disclose several types of ranges in the present invention.When Applicants disclose or claim a range of any type, Applicants'intent is to disclose or claim individually each possible number thatsuch a range could reasonably encompass, including end points of therange as well as any sub-ranges and combinations of sub-rangesencompassed therein. For example, when the Applicants disclose or claima chemical moiety having a certain number of carbon atoms, Applicants'intent is to disclose or claim individually every possible number thatsuch a range could encompass, consistent with the disclosure herein. Forexample, the disclosure that a moiety is a C₂ to C₁₈ alkenyl group, orin alternative language an alkenyl group having from 2 to 18 carbonatoms, as used herein, refers to a moiety that can be selectedindependently from an alkenyl group having 2, 3, 4, 5, 6, 7, 8, 9, 10,11, 12, 13, 14, 15, 16, 17, or 18 carbon atoms, as well as any rangebetween these two numbers (for example, a C₂ to C₈ alkenyl group), andalso including any combination of ranges between these two numbers (forexample, a C₂ to C₆ and a C₁₂ to C₁₆ alkenyl group).

Similarly, another representative example follows for the weight-averagemolecular weight (M_(w)) of an alpha olefin product produced in anaspect of this invention. By a disclosure that the M_(w) can be in arange from about 2,000 to about 150,000 g/mol, Applicants intend torecite that the M_(w) can be about 2,000, about 3,000, about 4,000,about 5,000, about 6,000, about 7,000, about 8,000, about 9,000, about10,000, about 20,000, about 30,000, about 40,000, about 50,000), about60,000, about 70,000, about 80,000, about 90,000, about 100,000), about110,000, about 120,000, about 130,000, about 140,000, or about 150,000g/mol. Additionally, the M_(w) can be within any range from about 2,000to about 150,000 (for example, from about 5,000 to about 50,000), andthis also includes any combination of ranges between about 2,000 andabout 150,000 (for example, the M_(w) can be in a range from about 4,000to about 25,000, or from about 50,000 to about 75,000). Likewise, allother ranges disclosed herein should be interpreted in a manner similarto these two examples.

Applicants reserve the right to proviso out or exclude any individualmembers of any such group, including any sub-ranges or combinations ofsub-ranges within the group, that can be claimed according to a range orin any similar manner, if for any reason Applicants choose to claim lessthan the full measure of the disclosure, for example, to account for areference that Applicants may be unaware of at the time of the filing ofthe application. Further, Applicants reserve the right to proviso out orexclude any individual substituents, analogs, compounds, ligands,structures, or groups thereof, or any members of a claimed group, if forany reason Applicants choose to claim less than the full measure of thedisclosure, for example, to account for a reference that Applicants maybe unaware of at the time of the filing of the application.

The following abbreviations are used in this disclosure:

-   -   Bn—benzyl    -   Et—ethyl    -   MAO—methylaluminoxane    -   Me—methyl    -   M_(w)—weight-average molecular weight    -   Ph—phenyl    -   t-Bu—tert-butyl    -   THF—tetrahydrofuran    -   TIBA—triisobutylaluminum

DETAILED DESCRIPTION OF THE INVENTION

The present invention is directed generally to new catalystcompositions, methods for preparing catalyst compositions, methods forusing the catalyst compositions to polymerize alpha olefins, the alphaolefin products produced using such catalyst compositions, and articlesproduced using alpha olefin products. In particular, the presentinvention relates to amine bis(phenolate) orN,N-bis[2-hydroxidebenzyl]amine transition metal compounds, and catalystcompositions employing such transition metal compounds.

Amine Bis(Phenolate) Transition Metal Complexes

The present invention discloses novel amine bis(phenolate) complexes orcompounds (e.g., N,N-bis[2-hydroxidebenzyl]amine complexes orcompounds), and methods of making these complexes or compounds. In anembodiment of this invention, the N,N-bis[2-hydroxidebenzyl]aminecompound can have the formula:

Within formula (Ia), M, X¹, X², R^(A), R^(B), R^(C), p, and q areindependent elements of the N,N-bis[2-hydroxidebenzyl]amine compound.Accordingly, the N,N-bis[2-hydroxidebenzyl]amine compound having formula(Ia) can be described using any combination of M, X¹, X², R^(A), R^(B),R^(C), p, and q disclosed herein.

Unless otherwise specified, formula (Ia) above, any other structuralformulas disclosed herein, and any N,N-bis[2-hydroxidebenzyl]aminecomplex, compound, or species disclosed herein are not designed to showstereochemistry or isomeric positioning of the different moieties (e.g.,these formulas are not intended to display cis or trans isomers, or R orS diastereoisomers), although such compounds are contemplated andencompassed by these formulas and/or structures.

In accordance with aspects of this invention, the metal in formula (Ia),M, can be Ti, Zr, or Hf. In one aspect, for instance, M can be Zr or Hf,while in another aspect, M can be Ti; alternatively, M can be Zr, oralternatively, M can be Hf.

X¹ and X² in formula (Ia) independently can be a monoanionic ligand. Insome aspects, suitable monoanionic ligands can include, but are notlimited to, H (hydride), BH₄, a halide, a C₁ to C₃₆ hydrocarbyl group, aC₁ to Ca hydrocarboxy group, a C₁ to C₃₆ hydrocarbylaminyl group, a C₁to C₃₆ hydrocarbylsilyl group, a C₁ to C₃₆ hydrocarbylaminylsilyl group,—OBR¹ ₂, or —OSO₂R¹, wherein R¹ is a C₁ to C₃₆ hydrocarbyl group. It iscontemplated that X¹ and X² can be either the same or a differentmonoanionic ligand.

In one aspect, X¹ and X² independently can be H, BH₄, a halide (e.g., F,Cl, Br, etc.), a C₁ to C₁₈ hydrocarbyl group, a C₁ to C₁₈ hydrocarboxygroup, a C₁ to C₁₈ hydrocarbylaminyl group, a C₁ to C₁₈ hydrocarbylsilylgroup, or a C₁ to C₁₈ hydrocarbylaminylsilyl group. Alternatively, X¹and X² independently can be H, BH₄, a halide, OBR¹ ₂, or OSO₂R¹, whereinR¹ is a C₁ to C₁₈ hydrocarbyl group. In another aspect, X¹ and X²independently can be H, BH₄, a halide, a C₁ to C₁₂ hydrocarbyl group, aC₁ to C₁₂ hydrocarboxy group, a C₁ to C₁₂ hydrocarbylaminyl group, a C₁to C₁₂ hydrocarbylsilyl group, a C₁ to C₁₂ hydrocarbylaminylsilyl group,OBR¹ ₂, or OSO₂R¹, wherein R¹ is a C₁ to C₁₀ hydrocarbyl group. In yetanother aspect. X¹ and X² independently can be H, BH₄, a halide, a C₁ toC₁₀ hydrocarbyl group, a C₁ to C₁₀ hydrocarboxy group, a C₁ to C₁₀hydrocarbylaminyl group, a C₁ to C₁₀ hydrocarbylsilyl group, a C₁ to C₁₀hydrocarbylaminylsilyl group. OBR¹ ₂, or OSO₂R¹, wherein R¹ is a C₁ toC₁₀ hydrocarbyl group. In still another aspect, X¹ and X² independentlycan be H, BH₄, a halide, a C₁ to C₈ hydrocarbyl group, a C₁ to C₈hydrocarboxy group, a C₁ to C₈ hydrocarbylaminyl group, a C₁ to C₈hydrocarbylsilyl group, a C₁ to C₈ hydrocarbylaminylsilyl group, OBR¹ ₂,or OSO₂R¹, wherein R¹ is a C₁ to C₈ hydrocarbyl group.

The hydrocarbyl group which can be X¹ and/or X² in formula (Ia) can be aC₁ to C₃₆ hydrocarbyl group, including, but not limited to, a C₁ to C₃₆alkyl group, a C₂ to C₃₆ alkenyl group, a C₄ to C₃₆ cycloalkyl group, aC₆ to C₃₆ aryl group, or a C₇ to C₃₆ aralkyl group. For instance, X¹ andX² independently can be a C₁ to C₁₈ alkyl group, a C₂ to C₁₈ alkenylgroup, a C₄ to C₁₈ cycloalkyl group, a C₆ to C₁₈ aryl group, or a C₇ toC₁₈ aralkyl group; alternatively, X¹ and X² independently can be a C₁ toC₁₂ alkyl group, a C₂ to C₁₂ alkenyl group, a C₄ to C₁₂ cycloalkylgroup, a C₆ to C₁₂ aryl group, or a C₇ to C₁₂ aralkyl group;alternatively, X¹ and X² independently can be a C₁ to C₁₀ alkyl group, aC₂ to C₁₀ alkenyl group, a C₄ to C₁₀ cycloalkyl group, a C₆ to C₁₀ arylgroup, or a C₇ to C₁₀ aralkyl group; or alternatively. X¹ and X²independently can be a C₁ to C₅ alkyl group, a C₂ to C₈ alkenyl group, aC₅ to C₈ cycloalkyl group, a C₆ to C₈ aryl group, or a C₇ to C₈ aralkylgroup.

Accordingly, in some aspects, the alkyl group which can be X¹ and/or X²in formula (Ia) can be a methyl group, an ethyl group, a propyl group, abutyl group, a pentyl group, a hexyl group, a heptyl group, an octylgroup, a nonyl group, a decyl group, a undecyl group, a dodecyl group, atridecyl group, a tetradecyl group, a pentadecyl group, a hexadecylgroup, a heptadecyl group, or an octadecyl group; or alternatively, amethyl group, an ethyl group, a propyl group, a butyl group, a pentylgroup, a hexyl group, a heptyl group, an octyl group, a nonyl group, ora decyl group. In some aspects, the alkyl group which can be X¹ and/orX² in formula (Ia) can be a methyl group, an ethyl group, a n-propylgroup, an iso-propyl group, a n-butyl group, an iso-butyl group, asec-butyl group, a tert-butyl group, a n-pentyl group, an iso-pentylgroup, a sec-pentyl group, or a neopentyl group; alternatively, a methylgroup, an ethyl group, an iso-propyl group, a tert-butyl group, or aneopentyl group; alternatively, a methyl group; alternatively, an ethylgroup; alternatively, a n-propyl group; alternatively, an iso-propylgroup; alternatively, a tert-butyl group; or alternatively, a neopentylgroup.

Suitable alkenyl groups which can be X¹ and/or X² in formula (Ia) caninclude, but are not limited to, an ethenyl group, a propenyl group, abutenyl group, a pentenyl group, a hexenyl group, a heptenyl group, anoctenyl group, a nonenyl group, a decenyl group, a undecenyl group, adodecenyl group, a tridecenyl group, a tetradecenyl group, apentadecenyl group, a hexadecenyl group, a heptadecenyl group, or anoctadecenyl group. Such alkenyl groups can be linear or branched, andthe double bond can be located anywhere in the chain. In one aspect, X¹and/or X² in formula (Ia) can be an ethenyl group, a propenyl group, abutenyl group, a pentenyl group, a hexenyl group, a heptenyl group, anoctenyl group, a nonenyl group, or a decenyl group, while in anotheraspect, X¹ and/or X² in formula (Ia) can be an ethenyl group, a propenylgroup, a butenyl group, a pentenyl group, or a hexenyl group. Forexample, X¹ and/or X² can be an ethenyl group; alternatively, a propenylgroup; alternatively, a butenyl group; alternatively, a pentenyl group;or alternatively, a hexenyl group. In yet another aspect, X¹ and/or X²can be a terminal alkenyl group, such as a C₃ to C₁₈ terminal alkenylgroup, a C₃ to C₁₂ terminal alkenyl group, or a C₃ to C₈ terminalalkenyl group. Illustrative terminal alkenyl groups can include, but arenot limited to, a prop-2-en-1-yl group, a bute-3-en-1-yl group, apent-4-en-1-yl group, a hex-5-en-1-yl group, a hept-6-en-1-yl group, anocte-7-en-1-yl group, a non-8-en-1-yl group, a dece-9-en-1-yl group, andso forth.

X¹ and/or X² in formula (Ia) can be a cycloalkyl group, including, butnot limited to, a cyclobutyl group, a substituted cyclobutyl group, acyclopentyl group, a substituted cyclopentyl group, a cyclohexyl group,a substituted cyclohexyl group, a cycloheptyl group, a substitutedcycloheptyl group, a cyclooctyl group, or a substituted cyclooctylgroup. For example, X¹ and/or X² in formula (Ia) can be a cyclopentylgroup, a substituted cyclopentyl group, a cyclohexyl group, or asubstituted cyclohexyl group. Moreover, X¹ and/or X² in formula (Ia) canbe a cyclobutyl group or a substituted cyclobutyl group; alternatively,a cyclopentyl group or a substituted cyclopentyl group; alternatively, acyclohexyl group or a substituted cyclohexyl group; alternatively, acycloheptyl group or a substituted cycloheptyl group; alternatively, acyclooctyl group or a substituted cyclooctyl group; alternatively, acyclopentyl group; alternatively, a substituted cyclopentyl group;alternatively, a cyclohexyl group; or alternatively, a substitutedcyclohexyl group. Substituents which can be utilized for the substitutedcycloalkyl group are independently disclosed herein and can be utilizedwithout limitation to further describe the substituted cycloalkyl groupwhich can be X¹ and/or X² in formula (Ia).

In some aspects, the aryl group which can be X¹ and/or X² in formula(Ia) can be a phenyl group, a substituted phenyl group, a naphthylgroup, or a substituted naphthyl group. In an aspect, the aryl group canbe a phenyl group or a substituted phenyl group; alternatively, anaphthyl group or a substituted naphthyl group; alternatively, a phenylgroup or a naphthyl group; alternatively, a substituted phenyl group ora substituted naphthyl group; alternatively, a phenyl group; oralternatively, a naphthyl group. Substituents which can be utilized forthe substituted phenyl groups or substituted naphthyl groups areindependently disclosed herein and can be utilized without limitation tofurther describe the substituted phenyl groups or substituted naphthylgroups which can be X¹ and/or X² in formula (Ia).

In an aspect, the substituted phenyl group which can be X¹ and/or X² informula (Ia) can be a 2-substituted phenyl group, a 3-substituted phenylgroup, a 4-substituted phenyl group, a 2,4-disubstituted phenyl group, a2,6-disubstituted phenyl group, a 3,5-disubstituted phenyl group, or a2,4,6-trisubstituted phenyl group. In other aspects, the substitutedphenyl group can be a 2-substituted phenyl group, a 4-substituted phenylgroup, a 2,4-disubstituted phenyl group, or a 2,6-disubstituted phenylgroup; alternatively, a 3-substituted phenyl group or a3,5-disubstituted phenyl group; alternatively, a 2-substituted phenylgroup or a 4-substituted phenyl group; alternatively, a2,4-disubstituted phenyl group or a 2,6-disubstituted phenyl group;alternatively, a 2-substituted phenyl group; alternatively, a3-substituted phenyl group; alternatively, a 4-substituted phenyl group;alternatively, a 2,4-disubstituted phenyl group; alternatively, a2,6-disubstituted phenyl group; alternatively, a 3,5-disubstitutedphenyl group; or alternatively, a 2,4,6-trisubstituted phenyl group.Substituents which can be utilized for these specific substituted phenylgroups are independently disclosed herein and can be utilized withoutlimitation to further describe these substituted phenyl groups which canbe the X¹ and/or X² group(s) in formula (Ia).

In some aspects, the aralkyl group which can be X¹ and/or X² group informula (Ia) can be a benzyl group or a substituted benzyl group. In anaspect, the aralkyl group can be a benzyl group or, alternatively, asubstituted benzyl group. Substituents which can be utilized for thesubstituted aralkyl group are independently disclosed herein and can beutilized without limitation to further describe the substituted aralkylgroup which can be the X¹ and/or X² group(s) in formula (Ia).

In an aspect, each non-hydrogen substituent(s) for the substitutedcycloalkyl group, substituted aryl group, or substituted aralkyl groupwhich can be X¹ and/or X² in formula (Ia) independently can be a C₁ toC₁₈ hydrocarbyl group; alternatively, a C₁ to C₈ hydrocarbyl group; oralternatively, a C₁ to C₁₈ hydrocarbyl group. Specific hydrocarbylgroups are independently disclosed herein and can be utilized withoutlimitation to further describe the substituents of the substitutedcycloalkyl groups, substituted aryl groups, or substituted aralkylgroups which can be X¹ and/or X² in formula (Ia). For instance, thehydrocarbyl substituent can be an alkyl group, such as a methyl group,an ethyl group, a n-propyl group, an isopropyl group, a n-butyl group, asec-butyl group, an isobutyl group, a tert-butyl group, a n-pentylgroup, a 2-pentyl group, a 3-pentyl group, a 2-methyl-1-butyl group, atert-pentyl group, a 3-methyl-1-butyl group, a 3-methyl-2-butyl group,or a neo-pentyl group, and the like. Furthermore, the hydrocarbylsubstituent can be a benzyl group, a phenyl group, a tolyl group, or axylyl group, and the like.

A hydrocarboxy group is used generically herein to include, forinstance, alkoxy, aryloxy, aralkoxy, and -(alkyl, aryl, oraralkyl)-O-(alkyl, aryl, or aralkyl) groups, and these groups cancomprise up to about 36 carbon atoms (e.g., C₁ to C₃₆, C₁ to C₁₈, C₁ toC₁₀, or C₁ to C₈ hydrocarboxy groups). Illustrative and non-limitingexamples of hydrocarboxy groups which can be X¹ and/or X² in formula(Ia) can include, but are not limited to, a methoxy group, an ethoxygroup, an n-propoxy group, an isopropoxy group, an n-butoxy group, asec-butoxy group, an isobutoxy group, a tert-butoxy group, an n-pentoxygroup, a 2-pentoxy group, a 3-pentoxy group, a 2-methyl-1-butoxy group,a tert-pentoxy group, a 3-methyl-1-butoxy group, a 3-methyl-2-butoxygroup, a neo-pentoxy group, a phenoxy group, a toloxy group, a xyloxygroup, a 2,4,6-trimethylphenoxy group, a benzoxy group, anacetylacetonate group (acac), and the like. In an aspect, thehydrocarboxy group which can be X¹ and/or X² in formula (Ia) can be amethoxy group; alternatively, an ethoxy group; alternatively, ann-propoxy group; alternatively, an isopropoxy group; alternatively, ann-butoxy group; alternatively, a sec-butoxy group; alternatively, anisobutoxy group; alternatively, a tert-butoxy group; alternatively, ann-pentoxy group; alternatively, a 2-pentoxy group; alternatively, a3-pentoxy group; alternatively, a 2-methyl-1-butoxy group;alternatively, a tert-pentoxy group; alternatively, a 3-methyl-1-butoxygroup, alternatively, a 3-methyl-2-butoxy group; alternatively, aneo-pentoxy group; alternatively, a phenoxy group; alternatively, atoloxy group; alternatively, a xyloxy group; alternatively, a2,4,6-trimethylphenoxy group; alternatively, a benzoxy group; oralternatively, an acetylacetonate group.

The term hydrocarbylaminyl group is used generically herein to refercollectively to, for instance, alkylaminyl, arylaminyl, aralkylaminyl,dialkylaminyl, diarylaminyl, diaralkylaminyl, and -(alkyl, aryl, oraralkyl)-N-(alkyl, aryl, or aralkyl) groups, and unless otherwisespecified, the hydrocarbylaminyl groups which can be X¹ and/or X² informula (Ia) can comprise up to about 36 carbon atoms (e.g., C₁ to C₃₆,C₁ to C₁₈, C₁ to C₁₀, or C₁ to C₈ hydrocarbylaminyl groups).Accordingly, hydrocarbylaminyl is intended to cover both(mono)hydrocarbylaminyl and dihydrocarbylaminyl groups. In some aspects,the hydrocarbylaminyl group which can be X¹ and/or X² in formula (Ia)can be, for instance, a methylaminyl group (—NHCH₃), an ethylaminylgroup (—NHCH₂CH₃), an n-propylaminyl group (—NHCH₂CH₂CH₃), aniso-propylaminyl group (—NHCH(CH₃)₂), an n-butylaminyl group(—NHCH₂CH₂CH₂CH₃), a t-butylaminyl group (—NHC(CH₃)₃), an n-pentylaminylgroup (—NHCH₂CH₂CHCH₂CH₃), a neo-pentylaminyl group (—NHCH₂C(CH₃)₃), aphenylaminyl group (—NHC₆H₅), a tolylaminyl group (—NHC₆H₄CH₃), or axylylaminyl group (—NHC₆H₃H(CH₃)₂); alternatively, a methylaminyl group;alternatively, an ethylaminyl group; alternatively, a propylaminylgroup; or alternatively, a phenylaminyl group. In other aspects, thehydrocarbylaminyl group which can be X¹ and/or X² in formula (Ia) canbe, for instance, a dimethylaminyl group (—N(CH₃)₂), a diethylaminylgroup (—N(CH₂CH₃)₂), a di-n-propylaminyl group (—N(CH₂CH₂CH₃)₂), adi-iso-propylaminyl group (—N(CH(CH₃)₂)₂), a di-n-butylaminyl group(—N(CH₂CH₂CH₂CH₃)₂), a di-t-butylaminyl group (—N(C(CH₃)₃)₂), adi-n-pentylaminyl group (—N(CH₂CH₂CH₂CH₂CH₃)₂), a di-no-pentylaminylgroup (—N(CH₂C(CH₃)₃)₂), a di-phenylaminyl group (—N(C₆H₅)₂), adi-tolylaminyl group (—N(C₆H₄CH₃)₂), or a di-xylylaminyl group(—N(C₆H₃(CH₃)₂)₂); alternatively, a dimethylaminyl group; alternatively,a di-ethylaminyl group; alternatively, a di-n-propylaminyl group; oralternatively, a di-phenylaminyl group.

In accordance with some aspects disclosed herein, one or both of X¹ andX² independently can be a C₁ to C₃₆ hydrocarbylsilyl group;alternatively, a C₁ to C₂₄ hydrocarbylsilyl group; alternatively, a C₁to C₁₈ hydrocarbylsilyl group; or alternatively, a C₁ to C₈hydrocarbylsilyl group. In an aspect, each hydrocarbyl (one or more) ofthe hydrocarbylsilyl group can be any hydrocarbyl group disclosed herein(e.g., a C₁ to C₅ alkyl group, a C₂ to C₅ alkenyl group, a C₅ to C₈cycloalkyl group, a C₆ to C₈ aryl group, a C₇ to C₈ aralkyl group,etc.). As used herein, hydrocarbylsilyl is intended to cover(mono)hydrocarbylsilyl (—SiH₂R), dihydrocarbylsilyl (—SiHR₂), andtrihydrocarbylsilyl (—SiR₃) groups, with R being a hydrocarbyl group. Inone aspect, the hydrocarbylsilyl group can be a C₃ to C₃₆ or a C₃ to C₁₈trihydrocarbylsilyl group, such as, for example, a trialkylsilyl groupor a triphenylsilyl group. Illustrative and non-limiting examples ofhydrocarbylsilyl groups which can be the X¹ and/or X² group(s) informula (Ia) can include, but are not limited to, trimethylsilyl,triethylsilyl, tripropylsilyl (e.g., triisopropylsilyl), tributylsilyl,tripentylsilyl, triphenylsilyl, allyldimethylsilyl, and the like.

A hydrocarbylaminylsilyl group is used herein to refer to groupscontaining at least one hydrocarbon moiety, at least one N atom, and atleast one Si atom. Illustrative and non-limiting examples ofhydrocarbylaminylsilyl groups which can be X¹ and/or X² can include, butare not limited to —N(SiMe₃)₂, —N(SiEt₃)₂, and the like. Unlessotherwise specified, the hydrocarbylaminylsilyl groups which can be X¹and/or X² can comprise up to about 36 carbon atoms (e.g., C₁ to C₃₆, C₁to C₁₈, C₁ to C₁₂, or C₁ to C₈ hydrocarbylaminylsilyl groups). In anaspect, each hydrocarbyl (one or more) of the hydrocarbylaminylsilylgroup can be any hydrocarbyl group disclosed herein (e.g., a C₁ to C₅alkyl group, a C₂ to C₅ alkenyl group, a C₅ to C₈ cycloalkyl group, a C₆to C₈ aryl group, a C₇ to C₈ aralkyl group, etc.). Moreover,hydrocarbylaminylsilyl is intended to cover —NH(SiH₂R), —NH(SiHR₂),—NH(SiR₃), —N(SiH₂R)₂, —N(SiHR₂)₂, —N(SiR₃)₂, groups, among others, withR being a hydrocarbyl group.

In an aspect, X¹ and X² independently can be —OBR¹ ₂ or —OSO₂R¹, whereinR¹ is a C₁ to C₃₆ hydrocarbyl group, or alternatively, a C₁ to C₁₈hydrocarbyl group. The hydrocarbyl group in OBR¹ ₂ and/or OSO₂R¹independently can be any hydrocarbyl group disclosed herein, such as,for instance, a C₁ to C₁₈ alkyl group, a C₂ to C₁₈ alkenyl group, a C₄to C₁₈ cycloalkyl group, a C₆ to C₁₈ aryl group, or a C₇ to C₁₈ aralkylgroup; a C₁ to C₁₂ alkyl group, a C₂ to C₁₂ alkenyl group, a C₄ to C₁₂cycloalkyl group, a C₆ to C₁₂ aryl group, or a C₇ to C₁₂ aralkyl group;or a C₁ to C₈ alkyl group, a C₂ to C₈ alkenyl group, a C₅ to C₈cycloalkyl group, a C₆ to C₈ aryl group, or a C₇ to C₈ aralkyl group.

In one aspect, X¹ and X² independently can be H, BH₄, a halide, or a C₁to C₃₆ hydrocarbyl group, hydrocarboxy group, hydrocarbylaminyl group,hydrocarbylsilyl group, or hydrocarbylaminylsilyl group, while inanother aspect, X¹ and X² independently can be H, BH₄, or a C₁ to C₁₈hydrocarboxy group, hydrocarbylaminyl group, hydrocarbylsilyl group, orhydrocarbylaminylsilyl group. In yet another aspect, X¹ and X²independently can be a halide; alternatively, a C₁ to C₁₈ hydrocarbylgroup; alternatively, a C₁ to C₁₈ hydrocarboxy group; alternatively, aC₁ to C₁₈ hydrocarbylaminyl group; alternatively, a C₁ to C₁₈hydrocarbylsilyl group; or alternatively, a C₁ to C₁₈hydrocarbylaminylsilyl group. In still another aspect, both X¹ and X²can be H; alternatively, F; alternatively, Cl; alternatively, Br;alternatively, I; alternatively, BH₄; alternatively, a C₁ to C₁₈hydrocarbyl group; alternatively, a C₁ to C₁₈ hydrocarboxy group;alternatively, a C₁ to C₁₈ hydrocarbylaminyl group; alternatively, a C₁to C₁₈ hydrocarbylsilyl group; or alternatively, a C₁ to C₁₈hydrocarbylaminylsilyl group.

X¹ and X² independently can be, in some aspects, H, a halide, methyl,phenyl, benzyl, an alkoxy, an aryloxy, acetylacetonate, an alkylaminyl,a dialkylaminyl, a trihydrocarbylsilyl, or a hydrocarbylaminylsilyl;alternatively, H, a halide, methyl phenyl, or benzyl; alternatively, analkoxy, an aryloxy, or acetylacetonate; alternatively, an alkylaminyl ora dialkylaminyl; alternatively, a trihydrocarbylsilyl orhydrocarbylaminylsilyl; alternatively, H or a halide; alternatively,methyl, phenyl, benzyl, an alkoxy, an aryloxy, acetylacetonate, analkylaminyl, or a dialkylaminyl; alternatively, H; alternatively, ahalide; alternatively, methyl; alternatively, phenyl; alternatively,benzyl; alternatively, an alkoxy; alternatively, an aryloxy;alternatively, acetylacetonate; alternatively, an alkylaminyl;alternatively, a dialkylaminyl; alternatively, a trihydrocarbylsilyl; oralternatively, a hydrocarbylaminylsilyl. In these and other aspects, thealkoxy, aryloxy, alkylaminyl, dialkylaminyl, trihydrocarbylsilyl, andhydrocarbylaminylsilyl can be a C₁ to C₃₆, a C₁ to C₁₈, a C₁ to C₁₂, ora C₁ to C₈ alkoxy, aryloxy, alkylaminyl, dialkylaminyl,trihydrocarbylsilyl, and hydrocarbylaminylsilyl.

Moreover, X¹ and X² independently can be, in certain aspects, a halideor a C₁ to C₁₈ hydrocarbyl group; alternatively, a halide or a C₁ to C₈hydrocarbyl group; alternatively, F, Cl, Br, I, methyl, benzyl, orphenyl; alternatively, Cl, methyl, benzyl, or phenyl; alternatively, aC, to C₁₈ alkoxy, aryloxy, alkylaminyl, dialkylaminyl,trihydrocarbylsilyl, or hydrocarbylaminylsilyl group; alternatively, aC₁ to C₈ alkoxy, aryloxy, alkylaminyl, dialkylaminyl,trihydrocarbylsilyl, or hydrocarbylaminylsilyl group; or alternatively,methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl,decyl, ethenyl, propenyl, butenyl, pentenyl, hexenyl, heptenyl, octenyl,nonenyl, decenyl, phenyl, tolyl, benzyl, naphthyl, trimethylsilyl,triisopropylsilyl, triphenylsilyl, or allyldimethylsilyl.

In formula (Ia), each R^(B) and/or R^(C) independently can be a halide,a C₁ to C₃₆ hydrocarbyl group, a C₁ to C₃₆ halogenated hydrocarbylgroup, a C₁ to C₃₆ hydrocarboxy group, or a C₁ to C₃₆ hydrocarbylsilylgroup. In some aspects, each R^(B) and/or R^(C) independently can be ahalide; alternatively, a C₁ to C₁₈ hydrocarbyl group; alternatively, aC₁ to C₁₈ halogenated hydrocarbyl group; alternatively, a C₁ to C₁₈hydrocarboxy group; or alternatively, a C₁ to C₁₈ hydrocarbylsilylgroup. Importantly, each R^(B) and/or R^(C) can be either the same or adifferent substituent group. Moreover, each R^(B) and/or R^(C) can be atany of the four positions of the respective ring structure shown informula (Ia). In an aspect, the number of R^(B)s and/or R^(C)s and/orthe positions of each R^(B) and/or R^(C) are independent of each other.For instance, two or more R^(B)s can be different, or alternatively, allR^(B)s can be the same. Additionally or alternatively, two or moreR^(C)s can be different, or alternatively, all R^(C)s can be the same.In another aspect, one or more of the R^(B)s can be different from theone or more of the R^(C)s, or alternatively, all R^(B)s can be the sameas the R^(C)s. In these and other aspects, each R^(B) and/or R^(C) canbe at any of the four positions of the respective ring structure shownin formula (Ia).

The halide, C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group,and C₁ to C₃₆ hydrocarbylsilyl group which can be a R^(B) and/or R^(C)in formula (Ia) can be any halide, C₁ to C₃₆ hydrocarbyl group, C₁ toC₃₆ hydrocarboxy group, and C₁ to C₃₆ hydrocarbylsilyl group describedherein (e.g., as pertaining to X¹ and X² in formula (Is)). A R^(B)and/or R^(C) in formula (Ia) can be, in certain aspects, a C₁ to C₃₆halogenated hydrocarbyl group, where the halogenated hydrocarbyl groupindicates the presence of one or more halogen atoms replacing anequivalent number of hydrogen atoms in the hydrocarbyl group. Thehalogenated hydrocarbyl group often can be a halogenated alkyl group, ahalogenated alkenyl group, a halogenated cycloalkyl group, a halogenatedaryl group, or a halogenated aralkyl group. Representative andnon-limiting halogenated hydrocarbyl groups include pentafluorophenyl,trifluoromethyl (CF₃), and the like.

As a non-limiting example, each R^(B) and/or R^(C) in formula (I)independently can be Cl, CF₃, a methyl group, an ethyl group, a propylgroup, a butyl group (e.g., t-Bu), a pentyl group, a hexyl group, aheptyl group, an octyl group, a nonyl group, a decyl group, an ethenylgroup, a propenyl group, a butenyl group, a pentenyl group, a hexenylgroup, a heptenyl group, an octenyl group, a nonenyl group, a decenylgroup, a phenyl group, a tolyl group (or other substituted aryl group),a benzyl group, a naphthyl group, a trimethylsilyl group, atriisopropylsilyl group, a triphenylsilyl group, or anallyldimethylsilyl group; alternatively, Cl; alternatively, CF₃;alternatively, a methyl group; alternatively, an ethyl group;alternatively, a propyl group; alternatively, a butyl group;alternatively, a pentyl group; alternatively, a hexyl group;alternatively, a heptyl group; alternatively, an octyl group, a nonylgroup; alternatively, a decyl group; alternatively, an ethenyl group;alternatively, a propenyl group; alternatively, a butenyl group;alternatively, a pentenyl group; alternatively, a hexenyl group;alternatively, a heptenyl group; alternatively, an octenyl group;alternatively, a nonenyl group; alternatively, a decenyl group;alternatively, a phenyl group; alternatively, a tolyl group;alternatively, a benzyl group; alternatively, a naphthyl group;alternatively, a trimethylsilyl group; alternatively, atriisopropylsilyl group; alternatively, a triphenylsilyl group; oralternatively, an allyldimethylsilyl group.

In formula (Ia), p can be 0, 1, 2, 3, or 4, and, independently, q can be0, 1, 2, 3, or 4. In some aspects, p can be 0, 1, or 2, and q can be 0,1, or 2, while in other aspects, p can be 0 or 2, and q can be 0 or 2.For instance, p can be equal to 0, q can be equal to 0, or both p and qcan be equal to 0. Alternatively, p can be equal to 2, q can be equal to2, or both p and q can be equal to 2. As noted above, each R^(B) and/orR^(C) can be either the same or a different substituent group. Forexample, when p is 2, 3, or 4, each R^(B) independently can be the sameor different.

R^(A) in formula (Ia) can be a C₁ to C₃₆ hydrocarbyl group or C₁ to C₁₆halogenated hydrocarbyl group, and these groups can be any C₁ to C₃₆hydrocarbyl group or C₁ to C₃₆ halogenated hydrocarbyl group describedherein (e.g., as pertaining to X¹, X², R^(B), and R^(C) in formula(Ia)). In some aspects, R^(A) can be a C₁ to C₂₄ hydrocarbyl group or aC₁ to C₂₄ halogenated hydrocarbyl group, while in other aspects, R^(A)can be a C₁ to C₁₈ hydrocarbyl group or a C₁ to C₁₈ halogenatedhydrocarbyl group. For example, R can be a C₁ to C₁₂ hydrocarbyl group,such as a C₁ to C₁₂ alkyl group, a C₁ to C₁₀ alkyl group, a C₁ to C₈alkyl group, a C₂ to C₈ alkyl group, a C₂ to C₁₂ alkenyl group, a C₂ toC₁₀ alkenyl group, a C₂ to C₈ alkenyl group, a C₃ to C₁₂ alkenyl group,a C₃ to C₁₀ alkenyl group, or a C₃ to C₈ alkenyl group, and the like. Inone aspect, R^(A) can be a methyl group, ethyl group, propyl group,butyl group, pentyl group, hexyl group, heptyl group, octyl group, nonylgroup, decyl group, ethenyl group, propenyl group, butenyl group,pentenyl group, hexenyl group, heptenyl group, octenyl group, nonenylgroup, decenyl group, phenyl group, tolyl group, benzyl group,phenylethyl group, or naphthyl group. In another aspect, R^(A) can be amethyl group, ethyl group, propyl group, butyl group, pentyl group,hexyl group, propenyl group, butenyl group, pentenyl group, hexenylgroup, phenyl group, benzyl group, or phenylethyl group. In yet anotheraspect, R^(A) can an ethenyl group, a propenyl group, a butenyl group, apentenyl group, a hexenyl group, a heptenyl group, an octenyl group, anonenyl group, a decenyl group, a undecenyl group, a dodecenyl group, atridecenyl group, a tetradecenyl group, a pentadecenyl group, ahexadecenyl group, a heptadecenyl group, or an octadecenyl group;alternatively, an ethenyl group, a propenyl group, a butenyl group, apentenyl group, a hexenyl group, a heptenyl group, an octenyl group, anonenyl group, or a decenyl group; alternatively, an ethenyl group, apropenyl group, a butenyl group, a pentenyl group, or a hexenyl group;alternatively, an ethenyl group; alternatively, a propenyl group;alternatively, a butenyl group; alternatively, a pentenyl group; oralternatively, a hexenyl group. In still another aspect, R^(A) can be aterminal alkenyl group, such as a C₃ to C₃₆ terminal alkenyl group, a C₃to C₂₄ terminal alkenyl group, a C₃ to C₁₈ terminal alkenyl group, a C₃to C₁₂ terminal alkenyl group, or a C₃ to C₈ terminal alkenyl group.

In another embodiment of this invention, theN,N-bis[2-hydroxidebenzyl]amine compound can have the formula:

Within formula (Ib), M, X¹, X², R^(A), R^(B1), R^(B2), R^(C1), andR^(C2) are independent elements of the N,N-bis[2-hydroxidebenzyl]aminecompound. Accordingly, the N,N-bis[2-hydroxidebenzyl]amine compoundhaving formula (Ib) can be described using any combination of M, X¹, X²,R^(A), R^(B1), R^(B2), R^(C1), and R^(C2) disclosed herein.

The selections for M, X¹, X², and R^(A) in formula (Ib) are the same asthose described herein above for formula (Ia). R^(B1), R^(B2), R^(C1),and R^(C2) independently can be a halide, C₁ to C₃₆ hydrocarbyl group,C₁ to C₃₆ halogenated hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group,or C₁ to C₃₆ hydrocarbylsilyl group, and these groups can be any halide,C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆ halogenated hydrocarbyl group, C₁to C₃₆ hydrocarboxy group, or C₁ to C₃₆ hydrocarbylsilyl group describedherein (e.g., as pertaining to R^(B) and R^(C) in formula (Ia)).

In one aspect, for example, R^(B1), R^(B2), R^(C1), and R^(C2)independently can be a methyl group, ethyl group, propyl group, butylgroup (e.g., t-Bu), pentyl group, hexyl group, propenyl group, butenylgroup, pentenyl group, hexenyl group, phenyl group, tolyl group, benzylgroup, trimethylsilyl group, triisopropylsilyl group, triphenylsilylgroup, allyldimethylsilyl group, CF₃, or Cl. In another aspect, R^(B1),R^(B2), R^(C1), and R^(C2) independently can be a methyl group, ethylgroup, propyl group, butyl group, pentyl group, hexyl group, propenylgroup, butenyl group, pentenyl group, hexenyl group, phenyl group, tolylgroup, or benzyl group. In yet another aspect, at least one of R^(B1),R^(B2), R^(C1), and R^(C2) (or alternatively, each of R^(B1), R^(B2),R^(C1), and R^(C2)) can be a methyl group; alternatively, an ethylgroup; alternatively, a propyl group; alternatively, a butyl group;alternatively, a pentyl group; alternatively, a hexyl group;alternatively, a propenyl group; alternatively, a butenyl group;alternatively, a pentenyl group; alternatively, a hexenyl group;alternatively, a phenyl group; alternatively, a tolyl group;alternatively, a benzyl group; alternatively, a trimethylsilyl group;alternatively, a triisopropylsilyl group; alternatively, atriphenylsilyl group; alternatively, an allyldimethylsilyl group;alternatively, CF₃; or alternatively, Cl. In these and other aspects,R^(A) in formula (Ib) can be a C₁ to C₁₈ hydrocarbyl group or C₁ to C₁₈halogenated hydrocarbyl group, examples of which can include, but arenot limited to, a methyl group, ethyl group, propyl group, butyl group,pentyl group, hexyl group, propenyl group, butenyl group, pentenylgroup, hexenyl group, phenyl group, benzyl group, phenylethyl group, andthe like.

Illustrative and non-limiting examples ofN,N-bis[2-hydroxidebenzyl]amine compounds having formula (Ia) andformula (Ib) can include, but are not limited to, compounds TM-1, TM-2,and TM-3 illustrated in FIG. 1.

Methods of making transition metal complexes of the present inventionalso are provided herein. Examples 1-8 that follow providerepresentative procedures for synthesizing compounds having formula (Ia)and formula (Ib), or for synthesizing precursor compounds useful in thesubsequent synthesis of compounds having formula (Ia) and formula (Ib).Additional methods for preparing compounds having formula (Ia) andformula (Ib) can be found in U.S. Pat. Nos. 6,333,423 and 6,596,827, thedisclosures of which are incorporated herein by reference in theirentirety. Using analogous synthesis schemes to those provided herein orknown to those of skill in the art, transition metal complexes similarto TM-1, TM-2, and TM-3, but with monoanionic ligands other than benzyl(e.g., halide, hydrocarbylaminyl, hydrocarbylsilyl, other hydrocarbyl,etc.), and/or with substituents other than tert-butyl (e.g., halide,hydrocarboxy, hydrocarbylsilyl, other hydrocarbyl, etc.), can bederived.

In another embodiment of this invention, theN,N-bis[2-hydroxidebenzyl]amine compound can have the formula:

Within formula (IIa), M, X¹, X², R^(B), R^(C), p, q, L, and D areindependent elements of the N,N-bis[2-hydroxidebenzyl]amine compound.Accordingly, the N,N-bis[2-hydroxidebenzyl]amine compound having formula(IIa) can be described using any combination of M, X¹, X², R^(B), R^(C),p, q, L, and D disclosed herein.

The selections for M, X¹, X², R^(B), R^(C), p, and q in formula (IIa)are the same as those described herein above for formula (Ia). Forinstance, M can be Ti, Zr, or Hf; alternatively, M can be Ti;alternatively, M can be Zr, or alternatively, M can be Hf. X¹ and X² informula (IIa) independently can be any monoanionic ligand disclosedherein, and this includes, but is not limited to, H, BH₄, a halide, a C₁to C₃₆ hydrocarbyl group, a C₁ to C₃₆ hydrocarboxy group, a C₁ to C₃₆hydrocarbylaminyl group, a C₁ to C₃₆ hydrocarbylsilyl group, a C₁ to C₃₆hydrocarbylaminylsilyl group, —OBR¹ ₂, or —OSO₂R¹, wherein R¹ is a C₁ toC₃₆ hydrocarbyl group. In some aspects, it is contemplated that X¹ andX² independently can be a C₁ to C₁₈ hydrocarbyl group, a C₁ to C₁₈hydrocarboxy group, a C₁ to C₁₈ hydrocarbylaminyl group, a C₁ to C₁₈hydrocarbylsilyl group, or a C₁ to C₁₈ hydrocarbylaminylsilyl group,while in other aspects, X¹ and X² independently can be a halide or a C₁to C₁₈ hydrocarbyl group. In formula (IIa), each R^(B) and/or R^(C)independently can be any halide, C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆halogenated hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group, or C₁ toC₃₆ hydrocarbylsilyl group disclosed herein. For example, each R^(B)and/or R^(C) independently can be Cl, CF₃, a methyl group, an ethylgroup, a propyl group, a butyl group (e.g., t-Bu), a pentyl group, ahexyl group, a heptyl group, an octyl group, a nonyl group, a decylgroup, an ethenyl group, a propenyl group, a butenyl group, a pentenylgroup, a hexenyl group, a heptenyl group, an octenyl group, a nonenylgroup, a decenyl group, a phenyl group, a tolyl group, a benzyl group, anaphthyl group, a trimethylsilyl group, a triisopropylsilyl group, atriphenylsilyl group, or an allyldimethylsilyl group. The integers, pand q, independently can be 0, 1, 2, 3, or 4, such as, for instance, pcan be 0, 1, or 2, and q can be 0, 1, or 2.

L in formula (IIa) can be a C₁ to C₁₈ hydrocarbylene group. Selectionsfor the C₁ to C₁₈ hydrocarbylene group can be any C₁ to C₁₈ hydrocarbylgroup disclosed herein from which another hydrogen atom can be removed.In one aspect, the hydrocarbylene group which can be L in formula (IIa)can be a C₁ to C₁₈ alkylene group, a C₄ to C₁₈ cycloalkylene group, a C₆to C₁₈ arylene group, or a C₇ to C₁₈ aralkylene group. In anotheraspect, L can be a C₂ to C₁₈ hydrocarbylene group, a C₂ to C₁₅hydrocarbylene group, a C₂ to C₈ hydrocarbylene group, a C₂ to C₄hydrocarbylene group, a C₁ to C₁₅ hydrocarbylene group, a C₁ to C₈hydrocarbylene group, or a C₁ to C₄ hydrocarbylene group. In yet anotheraspect, L can be a C₁ to C₁₅ alkylene group, a C₄ to C₁₅ cycloalkylenegroup, a C₆ to C₁₈ arylene group, or a C₁ to C₁₅ aralkylene group;alternatively, a C₁ to C₁₂ alkylene group, a C₄ to C₁₂ cycloalkylenegroup, a C₆ to C₁₂ arylene group, or a C₇ to C₁₂ aralkylene group;alternatively, a C₁ to C₁₀ alkylene group, a C₄ to C₁₀ cycloalkylenegroup, a C₆ to C₁₀ arylene group, or a C₇ to C₁₀ aralkylene group; oralternatively, a C₂ to C₅ alkylene group, a C₅ to C₈ cycloalkylenegroup, a C₆ to C₈ arylene group, or a C₇ to C₈ aralkylene group.

In some aspects, the alkylene group which can be L in formula (IIa) canbe a methylene group, an ethylene group, a propylene group, a butylenegroup, a pentylene group, a hexylene group, a heptylene group, anoctylene group, a nonylene group, a decylene group, a undecylene group,a dodecylene group, a tridecylene group, a tetradecylene group, apentadecylene group, a hexadecylene group, a heptadecylene group, or anoctadecylene group; alternatively, a methylene group, an ethylene group,a propylene group, a butylene group, a pentylene group, a hexylenegroup, a heptylene group, an octylene group, a nonylene group, or adecylene group; alternatively, a methylene group, an ethylene group, apropylene group, a butylene group, or a pentylene group. In otheraspects, L can be a methylene group; alternatively, an ethylene group(—CH₂CH₂—); alternatively, a propylene group; alternatively, a butylenegroup; alternatively, a pentylene group; alternatively, a hexylenegroup; alternatively, a heptylene group; alternatively, an octylenegroup; alternatively, a nonylene group; alternatively, a decylene group;alternatively, a undecylene group; alternatively, a dodecylene group;alternatively, a tridecylene group; alternatively, a tetradecylenegroup; alternatively, a pentadecylene group; alternatively, ahexadecylene group; alternatively, a heptadecylene group; oralternatively, an octadecylene group. Moreover, L can be aneth-1,2-ylene group, a prop-1,3-ylene group, a but-1,4-ylene group, abut-2,3-ylene group, a pent-1,5-ylene group, a2,2-dimethylprop-1,3-ylene group, a hex-1,6-ylene group, or a2,3-dimethylbut-2,3-ylene group; alternatively, an eth-1,2-ylene group,a prop-1,3-ylene group, a but-1,4-ylene group, a pent-1,5-ylene group,or a hex-1,6-ylene group; alternatively, an eth-1,2-ylene group;alternatively, a prop-1,3-ylene group; alternatively, a but-1,4-ylenegroup; alternatively, a but-2,3-ylene group; alternatively, apent-1,5-ylene group; alternatively, a 2,2-dimethylprop-1,3-ylene group;alternatively, a hex-1,6-ylene group; or alternatively, a2,3-dimethylbut-2,3-ylene group.

L in formula (IIa) can be a cycloalkylene group, including, but notlimited to, a cyclobutylene group, a substituted cyclobutylene group, acyclopentylene group, a substituted cyclopentylene group, acyclohexylene group, a substituted cyclohexylene group, a cycloheptylenegroup, a substituted cycloheptylene group, a cyclooctylene group, or asubstituted cyclooctylene group. For example, L can be a cyclobutylenegroup or a substituted cyclobutylene group; alternatively, acyclopentylene group or a substituted cyclopentylene group;alternatively, a cyclohexylene group or a substituted cyclohexylenegroup; alternatively, a cycloheptylene group or a substitutedcycloheptylene group; alternatively, a cyclooctylene group or asubstituted cyclooctylene group; alternatively, a cyclopentylene group;alternatively, a substituted cyclopentylene group; alternatively, acyclohexylene group; or alternatively, a substituted cyclohexylenegroup. In an aspect, L can be a cyclopent-1,3-ylene group, a substitutedcyclopent-1,3-ylene group, a cyclohex-1,3-ylene group, a substitutedcyclohex-1,3-ylene group, a cyclohex-1,4-ylene group, or a substitutedcyclohex-1,4-ylene group; alternatively, a cyclopent-1,3-ylene group, acyclohex-1,3-ylene group, or a cyclohex-1,4-ylene group. In anotheraspect, L can be a cyclopent-1,3-ylene group or a substitutedcyclopent-1,3-ylene group; alternatively, a cyclohex-1,3-ylene group, asubstituted cyclohex-1,3-ylene group, a cyclohex-1,4-ylene group, or asubstituted cyclohex-1,4-ylene group; alternatively, acyclohex-1,3-ylene group or a substituted cyclohex-1,3-ylene group;alternatively, a cyclohex-1,4-ylene group or a substitutedcyclohex-1,4-ylene group; alternatively, a cyclopent-1,3-ylene group, acyclohex-1,3-ylene group, or a cyclohex-1,4-ylene group; oralternatively, a substituted cyclopent-1,3-ylene group, a substitutedcyclohex-1,3-ylene group, or a substituted cyclohex-1,4-ylene group. Inanother aspect, L can be a cyclopent-1,3-ylene group; alternatively, asubstituted cyclopent-1,3-ylene group; alternatively, acyclohex-1,3-ylene group; alternatively, a substitutedcyclohex-1,3-ylene group; alternatively, a cyclohex-1,4-ylene group; oralternatively, a substituted cyclohex-1,4-ylene group. In anotheraspect, L can be a 2-substituted cyclopen-1,3-ylene group, a4,5-disubstituted cyclopen-1,3-ylene group, a 2,5-disubstitutedcyclopen-1,3-ylene group, or a 2,4,5-trisubstituted cyclopen-1,3-ylenegroup; alternatively, a 2-substituted cyclopen-1,3-ylene group;alternatively, a 4,5-disubstituted cyclopen-1,3-ylene group;alternatively, a 2,5-disubstituted cyclopen-1,3-ylene group;alternatively, a 2,4,5-trisubstituted cyclopen-1,3-ylene group. Inanother aspect, L can be a 2,6-disubstituted cyclohex-1,4-ylene group, a2,3-disubstituted cyclohex-1,4-ylene group, a 2,5-disubstitutedcyclohex-1,4-ylene group, or a 2,3,5,6-tetrasubstitutedcyclohex-1,4-ylene group. In another aspect, L can be a2,6-disubstituted cyclohex-1,4-ylene group or a 2,5-disubstitutedcyclohex-1,4-ylene group; alternatively, a 2,6-disubstitutedcyclohex-1,4-ylene group; alternatively, a 2,3-disubstitutedcyclohex-1,4-ylene group; alternatively, a 2,5-disubstitutedcyclohex-1,4-ylene group; or alternatively, a 2,3,5,6-tetrasubstitutedcyclohex-1,4-ylene group. In yet another aspect, L can be a2-substituted cyclohex-1,3-ylene group, a 2,4-disubstitutedcyclohex-1,3-ylene group, a 4,6-disubstituted cyclohex-1,3-ylene group,or a 2,4,6-trisubstituted cyclohex-1,3-ylene group. In still anotheraspect, L can be a 2-substituted cyclohex-1,3-ylene group;alternatively, a 2,4-disubstituted cyclohex-1,3-ylene group;alternatively, a 4,6-disubstituted cyclohex-1,3-ylene group; oralternatively, a 2,4,6-trisubstituted cyclohex-1,3-ylene group. Thesubstituent(s) for a substituted cycloalkylene group in formula (IIa)can be any substituent (e.g., a C₁ to C₁₂ hydrocarbyl group, a C₁ to C₈alkyl group, etc.) disclosed herein above, e.g., in relation tosubstituted cycloalkyl groups in formula (Ia).

In formula (IIa), L can be an arylene group, e.g., a phenylene group, asubstituted phenylene group, a naphthylene group, or a substitutednaphthylene group. In one aspect, L can be a phenylene group;alternatively, a substituted phenylene group; alternatively, anaphthylene group; or alternatively, a substituted naphthylene group. Inanother aspect, L can be a phen-1,2-ylene group or a substitutedphen-1,2-ylene group; alternatively, a phen-1,2-ylene group; oralternatively, a substituted phen-1,2-ylene group. In another aspect, Lcan be a phen-1,3-ylene group or a substituted phen-1,3-ylene group;alternatively, a phen-1,3-ylene group; or alternatively, a substitutedphen-1,3-ylene group. In another aspect, L can be a phen-1,4-ylene groupor a substituted phen-1,4-ylene group; alternatively, a phen-1,4-ylenegroup; or alternatively, a substituted phen-1,4-ylene group. In anotheraspect, L can be a phen-1,2-ylene group, a phen-1,3-ylene group, or aphen-1,4-ylene group; alternatively, a phen-1,3-ylene group or aphen-1,4-ylene group. In another aspect, L can be a substitutedphen-1,2-ylene group, a substituted phen-1,3-ylene group, or asubstituted phen-1,4-ylene group; alternatively, a substitutedphen-1,3-ylene group or a substituted phen-1,4-ylene group. In anotheraspect, L can be a 2,6-disubstituted phen-1,4-ylene group, a2,3-disubstituted phen-1,4-ylene group, a 2,5-disubstitutedphen-1,4-ylene group, or a 2,3,5,6-tetrasubstituted phen-1,4-ylenegroup. In another aspect, L can be a 2,6-disubstituted phen-1,4-ylenegroup or a 2,5-disubstituted phen-1,4-ylene group; alternatively, a2,6-disubstituted phen-1,4-ylene group; alternatively, a2,3-disubstituted phen-1,4-ylene group; alternatively, a2,5-disubstituted phen-1,4-ylene group; or alternatively, a2,3,5,6-tetrasubstituted phen-1,4-ylene group. In yet another aspect, Lcan be a 2-substituted phen-1,3-ylene group, a 2,4-disubstitutedphen-1,3-ylene group, a 4,6-disubstituted phen-1,3-ylene group, or a2,4,6-trisubstituted phen-1,3-ylene group. In still another aspect, Lcan be a 2-substituted phen-1,3-ylene group; alternatively, a2,4-disubstituted phen-1,3-ylene group; alternatively, a4,6-disubstituted phen-1,3-ylene group; or alternatively, a2,4,6-trisubstituted phen-1,3-ylene group. In some aspects, L can be anaphth-1,3-ylene group, a substituted naphth-1,3-ylene group, anaphth-1,4-ylene group, a substituted naphth-1,4-ylene group, anaphth-1,5-ylene group, a substituted naphth-1,5-ylene group, anaphth-1,6-ylene group, a substituted naphth-1,6-ylene group, anaphth-1,7-ylene group, a substituted naphth-1,7-ylene group, anaphth-1,8-ylene group, or a substituted naphth-1,8-ylene group. Inother aspects, L can be a naphth-1,3-ylene group or a substitutednaphth-1,3-ylene group; alternatively, a naphth-1,4-ylene group or asubstituted naphth-1,4-ylene group; alternatively, a naphth-1,5-ylenegroup or a substituted naphth-1,5-ylene group; alternatively, anaphth-1,6-ylene group or a substituted naphth-1,6-ylene group;alternatively, a naphth-1,7-ylene group or a substitutednaphth-1,7-ylene group; or alternatively, a naphth-1,8-ylene group or asubstituted naphth-1,8-ylene group. Yet, in other aspects, L can be anaphth-1,3-ylene group; alternatively, a substituted naphth-1,3-ylenegroup; alternatively, a naphth-1,4-ylene group; alternatively, asubstituted naphth-1,4-ylene group; alternatively, a naphth-1,5-ylenegroup; alternatively, a substituted naphth-1,5-ylene group;alternatively, a naphth-1,6-ylene group; alternatively, a substitutednaphth-1,6-ylene group; alternatively, a naphth-1,7-ylene group;alternatively, a substituted naphth-1,7-ylene group; alternatively, anaphth-1,8-ylene group; or alternatively, a substituted naphth-1,8-ylenegroup. The substituent(s) for a substituted arylene group in formula(IIa) can be any substituent (e.g., a C₁ to C₁₂ hydrocarbyl group, a C₁to C₈ alkyl group, etc.) disclosed herein above, e.g., in relation tosubstituted aryl groups in formula (Ia).

In an aspect, L can be a di(methylene)benzene group or a substituteddi(methylene)benzene group; or alternatively, a di(methylene) benzenegroup. In another aspect, L can be a 1,2-di(methylene)benzene group, asubstituted 1,2-di(methylene)benzene group, a 1,3-di(methylene)benzenegroup, a substituted 1,3-di(methylene)benzene group, a1,4-di(methylene)benzene group, or a substituted1,4-di(methylene)benzene group; alternatively, a1,2-di(methylene)benzene group, a 1,3-di(methylene)benzene group, or a1,4-di(methylene)benzene group. In yet another aspect, L can be a1,2-di(methylene)benzene group or a substituted 1,2-di(methylene)benzenegroup; alternatively, a 1,3-di(methylene)benzene group or a substituted1,3-di(methylene)benzene group; alternatively, a1,4-di(methylene)benzene group or a substituted 1,4-di(methylene)benzenegroup; alternatively, a 1,2-di(methylene)benzene group; alternatively, a1,3-di(methylene)benzene group; or alternatively, a1,4-di(methylene)benzene group. The substituent(s) for a substituteddi(methylene)benzene group in formula (IIa) can be any substituent(e.g., a C₁ to C₁₂ hydrocarbyl group, a C₁ to C₈ alkyl group, etc.)disclosed herein above, e.g., in relation to substituted aryl groups informula (Ia).

In formula (IIa), D can be a chemical group comprising at least one ofnitrogen, oxygen, phosphorus, and sulfur. In some aspects, theheteroatom-containing D group can complex and/or coordinate with themetal, M. D can be a C₁ to C₃₆ group comprising at least one ofnitrogen, oxygen, phosphorus, and sulfur; alternatively, a C₁ to C₂₄group comprising at least one of nitrogen, oxygen, phosphorus, andsulfur; alternatively, a C₁ to C₁₈ group comprising at least one ofnitrogen, oxygen, phosphorus, and sulfur; alternatively, a C₁ to C₁₀group comprising at least one of nitrogen, oxygen, phosphorus, andsulfur; or alternatively, a C₁ to C₅ group comprising at least one ofnitrogen, oxygen, phosphorus, and sulfur. In some aspects, theheteroatom can be oxygen; alternatively, sulfur; alternatively,nitrogen; alternatively, phosphorus; alternatively, nitrogen and oxygen;or alternatively, nitrogen and sulfur. Hence, D can contain more thanone heteroatom (e.g., nitrogen and oxygen, two nitrogens, etc.).Optionally, D can contain inert heteroatoms other than nitrogen, oxygen,phosphorus, and sulfur, which do not complex and/or coordinate with themetal (e.g., halides or silicon).

In an aspect, D can be a dihydrocarbyl aminyl group, a dihydrocarbylphosphinyl group, a hydrocarbyl etheryl group, or a hydrocarbyl sulfidylgroup. In another aspect, D can be a dihydrocarbyl aminyl group;alternatively, a dihydrocarbyl phosphinyl group; alternatively, ahydrocarbyl etheryl group; or alternatively, a hydrocarbyl sulfidylgroup. In these and other aspects, each hydrocarbyl group of thedihydrocarbyl aminyl group, the dihydrocarbyl phosphinyl group, thehydrocarbyl etheryl group, and the hydrocarbyl sulfidyl group can be anyhydrocarbyl group disclosed herein, such as, for example, an alkylgroup, an alkenyl group, a cycloalkyl group, an aryl group, or anaralkyl group; alternatively, an alkyl group; alternatively, an alkenylgroup; alternatively, a cycloalkyl group; alternatively, an aryl group;or alternatively, an aralkyl group. Suitable alkyl groups, alkenylgroups, cycloalkyl groups, aryl groups, and aralkyl groups areindependently disclosed herein and can be utilized without limitation tofurther describe D in formula (IIa).

In accordance with an aspect of the invention, D can be a dialkylaminylgroup, a dicycloalkylaminyl group, a di(substituted cycloalkyl)aminylgroup, an N-(alkyl)-N-(cycloalkyl)aminyl group, anN-(alkyl)-N-(substituted cycloalkyl)aminyl group, anN-(cycloalkyl)-N-(substituted cycloalkyl)aminyl group, a diarylaminylgroup, a di(substituted aryl)aminyl group, an N-aryl N-(substitutedaryl)aminyl group, an N-alkyl N-arylaminyl group, an N-alkylN-(substituted aryl)aminyl group, a dialkylphosphinyl group, adicycloalkylphosphinyl group, a di(substituted cycloalkyl)phosphinylgroup), an N (alkyl)-N-(cycloalkyl)phosphinyl group, anN-(alkyl)-N-(substituted cycloalkyl)phosphinyl group, anN-(cycloalkyl)-N-(substituted cycloalkyl)phosphinyl group, adiarylphosphinyl group, a di(substituted aryl)phosphinyl group, a P-arylP-(substituted aryl)phosphinyl group, a P-alkyl P-arylphosphinyl group,a P-alkyl P-(substituted aryl)phosphinyl group, an alkoxy group, anaroxy group, a substituted aroxy group, an alkylsulfidyl group, anarylsulfidyl group, a substituted arylsulfidyl group, a furanyl group, asubstituted furanyl group, a thienyl group, a substituted thienyl group,a tetrahydrofuranyl group, a substituted tetrahydrofuranyl group, athiophanyl group, a substituted thiophanyl group, a pyridinyl group, asubstituted pyridinyl group, a morphilinyl group, a substitutedmorphilinyl group, a pyranyl group, a substituted pyranyl group, atetrahydropyranyl group, a substituted tetrahydropyranyl group, aquinolinyl group, a substituted quinolinyl group, a pyrrolyl group, asubstituted pyrrolyl group, a pyrrolidinyl group, a substitutedpyrrolidinyl group, a piperidinyl group, or a substituted piperidinylgroup. For any of the cyclic or heterocyclic groups, L can bond to anyposition of the respective ring structure that is consistent with therules of chemical valence. For any of the substituted groups, thesubstituent(s) can be any substituent (e.g., a C₁ to C₁₂ hydrocarbylgroup, a C₁ to C₈ alkyl group, etc.) disclosed herein, such as above inrelation to substituted groups pertaining to formula (Ia). Similarly,the alkyl, cycloalkyl, aryl, and aralkyl groups can be any alkyl,cycloalkyl, aryl, and aralkyl, groups disclosed herein.

In another aspect, D can be a dialkylaminyl group, a dicycloalkylaminylgroup, a di(substituted cycloalkyl)aminyl group, anN-(alkyl)-N-(cycloalkyl)aminyl group, an N-(alkyl)-N-(substitutedcycloalkyl)aminyl group, an N-(cycloalkyl)-N-(substitutedcycloalkyl)aminyl group, a diarylaminyl group, a di(substitutedaryl)aminyl group, an N-aryl N-(substituted aryl)aminyl group, anN-alkyl N-arylaminyl group, or an N-alkyl N-(substituted aryl)aminylgroup. In another aspect. D can be a dialkylphosphinyl group, adicycloalkylphosphinyl group, a di(substituted cycloalkyl)phosphinylgroup), an N (alkyl)-N-(cycloalkyl)phosphinyl group, anN-(alkyl)-N-(substituted cycloalkyl)phosphinyl group, anN-(cycloalkyl)-N-(substituted cycloalkyl)phosphinyl group, adiarylphosphinyl group, a di(substituted aryl)phosphinyl group, a P-arylP-(substituted aryl)phosphinyl group, a P-alkyl P-arylphosphinyl group,or a P-alkyl P-(substituted aryl)phosphinyl group. In another aspect, Dcan be an alkoxy group, an aroxy group, or a substituted aroxy group.Yet, in another aspect, D can be an alkylsulfidyl group, an arylsulfidylgroup, or a substituted arylsulfidyl group. In still another aspect, Dcan be a furanyl group, a substituted furanyl group, a thienyl group, asubstituted thienyl group, a tetrahydrofuranyl group, a substitutedtetrahydrofuranyl group, a thiophanyl group, a substituted thiophanylgroup, a pyridinyl group, a substituted pyridinyl group, a morphilinylgroup, a substituted morphilinyl group, a pyranyl group, a substitutedpyranyl group, a tetrahydropyranyl group, a substitutedtetrahydropyranyl group, a quinolinyl group, a substituted quinolinylgroup, a pyrrolyl group, a substituted pyrrolyl group, a pyrrolidinylgroup, a substituted pyrrolidinyl group, a piperidinyl group, or asubstituted piperidinyl group.

In another aspect, D can be a dialkylaminyl group; alternatively, adicycloalkylaminyl group; alternatively, a di(substitutedcycloalkyl)aminyl group; alternatively, anN-(alkyl)-N-(cycloalkyl)aminyl group; alternatively, anN-(alkyl)-N-(substituted cycloalkyl)aminyl group; alternatively, anN-(cycloalkyl)-N-(substituted cycloalkyl)aminyl group; alternatively, adiarylaminyl group; alternatively, a di(substituted aryl)aminyl group;alternatively, an N-aryl N-(substituted aryl)aminyl group;alternatively, an N-alkyl N-arylaminyl group; alternatively, an N-alkylN-(substituted aryl)aminyl group; alternatively, a dialkylphosphinylgroup; alternatively, a dicycloalkylphosphinyl group; alternatively, adi(substituted cycloalkyl)phosphinyl group); alternatively, an N(alkyl)-N-(cycloalkyl)phosphinyl group; alternatively, anN-(alkyl)-N-(substituted cycloalkyl)phosphinyl group; alternatively, anN-(cycloalkyl)-N-(substituted cycloalkyl)phosphinyl group;alternatively, a diarylphosphinyl group; alternatively, a di(substitutedaryl)phosphinyl group; alternatively, a P-aryl P-(substitutedaryl)phosphinyl group; alternatively, a P-alkyl P-arylphosphinyl group;alternatively, a P-alkyl P-(substituted aryl)phosphinyl group;alternatively, an alkoxy group; alternatively, an aroxy group;alternatively, a substituted aroxy group; alternatively, analkylsulfidyl group; alternatively, an arylsulfidyl group;alternatively, a substituted arylsulfidyl group; alternatively, afuranyl group; alternatively, a substituted furanyl group;alternatively, a thienyl group; alternatively, a substituted thienylgroup; alternatively, a tetrahydrofuranyl group; alternatively, asubstituted tetrahydrofuranyl group; alternatively, a thiophanyl group;alternatively, a substituted thiophanyl group; alternatively, apyridinyl group; alternatively, a substituted pyridinyl group;alternatively, a morphilinyl group; alternatively, a substitutedmorphilinyl group; alternatively, a pyranyl group; alternatively, asubstituted pyranyl group; alternatively, a tetrahydropyranyl group;alternatively, a substituted tetrahydropyranyl group; alternatively, aquinolinyl group; alternatively, a substituted quinolinyl group;alternatively, a pyrrolyl group; alternatively, a substituted pyrrolylgroup; alternatively, a pyrrolidinyl group; alternatively, a substitutedpyrrolidinyl group; alternatively, a piperidinyl group; oralternatively, a substituted piperidinyl group.

In an aspect. D in formula (IIa) can have Structure Q1, Structure Q2,Structure Q3, Structure Q4, Structure Q5, Structure Q6, Structure Q7,Structure Q8, Structure Q9, Structure Q10, Structure Q11, Structure Q12,Structure Q13, Structure Q14, Structure Q15, Structure Q16, StructureQ17, Structure Q18, Structure Q19, Structure Q20, Structure Q21, orStructure Q22, and these structures are illustrated in the table below.

Table of Structures Q1 to Q22 —OR^(q1) Structure Q1 —SR^(q2) StructureQ2 —NR^(q3)R^(q4) Structure Q3 —PR^(q5)R^(q6) Structure Q4

Structure Q5

Structure Q6

Structure Q7

Structure Q8

Structure Q9

Structure Q10

Structure Q11

Structure Q12

Structure Q13

Structure Q14

Structure Q15

Structure Q16

Structure Q17

Structure Q18

Structure Q19

Structure Q20

Structure Q21

Structure Q22

In another aspect, D can have Structure Q1, Structure Q2, Structure Q3,Structure Q4, Structure Q5, Structure Q6, Structure Q7, Structure Q8,Structure Q9, Structure Q10, Structure Q11, Structure Q12, StructureQ13, Structure Q16, Structure Q17, Structure Q18, Structure Q19, orStructure Q20. In yet another aspect, D can have Structure Q1, StructureQ2, Structure Q3, or Structure Q4; alternatively, Structure Q1 orStructure Q2; alternatively, Structure Q3 or Structure Q4;alternatively, Structure Q5 or Structure Q6; alternatively, Structure Q7or Structure Q10; alternatively, Structure Q8 or Structure Q9;alternatively, Structure Q11 or Structure Q12; alternatively, StructureQ11 or Structure Q13; alternatively, Structure Q19 or Structure Q20;alternatively, Structure Q1; alternatively, Structure Q2; alternatively,Structure Q3; alternatively, Structure Q4; alternatively, Structure Q5;alternatively, Structure Q6; alternatively, Structure Q7; alternatively,Structure Q8; alternatively. Structure Q9; alternatively, Structure Q10;alternatively, Structure Q11; alternatively, Structure Q12;alternatively, Structure Q13; alternatively, Structure Q16;alternatively, Structure Q17; alternatively, Structure Q18;alternatively, Structure Q19; or alternatively, Structure Q20. In stillanother aspect, D can have Structure Q14, Structure Q15, Structure Q21,or Structure Q22; alternatively, Structure Q14 or Structure Q15;alternatively, Structure Q21 or Structure Q22; alternatively, StructureQ14; alternatively, Structure Q15; alternatively, Structure Q21; oralternatively, Structure Q22.

In some aspects, R^(q1), R^(q2), R^(q3), R^(q4), R^(q5), and R^(q6)within Structure Q1, Structure Q2, Structure Q3, or Structure Q4 can beany C₁ to C₁₈ hydrocarbyl group, C₁ to C₁, hydrocarbyl group, C₁ to C₁₀hydrocarbyl group, or C₁ to C₅ hydrocarbyl group disclosed herein. Forinstance, R^(q1), R^(q2), R^(q3), R^(q4), R^(q5), and R^(q6) withinStructure Q1, Structure Q2, Structure Q3, or Structure Q4 independentlycan be any C₁ to C₁₈ alkyl group, C₄ to C₁₈ cycloalkyl group, C₆ to C₁₈aryl group, C₁ to C₁₈ aralkyl group, or C₂ to C₁₈ alkenyl groupdisclosed herein, or any C₁ to C₅ alkyl group, C₄ to C₈ cycloalkylgroup, C₆ to C₁₀ aryl group, C₇ to C₁₀ aralkyl group, or C₃ to C₈alkenyl group (e.g., propenyl, butenyl, pentenyl, etc.) disclosedherein. In a similar manner, R^(q21) in Structure Q8, Structure Q9, andStructure Q10 can be any C₁ to C₁₈ hydrocarbyl group (e.g., alkyl group,cycloalkyl group, aryl group, aralkyl group, alkenyl group, etc.)disclosed herein.

In some aspects, each R^(q11), R^(q12), R^(q13), R^(q14), R^(q15),R^(q16), R^(q17), R^(q18), R^(q19), R^(q20), R^(q31), R^(q32), R^(q33),R^(q34), R^(q35), R^(q41), R^(q42), R^(q43), R^(q44), R^(q45), R^(q51),R^(q52), R^(q53), R^(q54), R^(q61), R^(q62), R^(q63), R^(q71), R^(q72),R^(q73), R^(q74), R^(q75), R^(q76), R^(q77), R^(q78), R^(q79), and/orR^(q80) of Structures Q5-Q22 independently can be hydrogen or any C₁ toC₁₈ hydrocarbyl group disclosed herein. Accordingly, eachR^(q11)-R^(q20), R^(q31)-R^(q35), R^(q41)-R^(q45), R^(q51)-R^(q54),R^(q61)-R^(q63), and/or R^(q71)-R^(q80) non-hydrogen substituent inStructures Q5-Q22 can be any alkyl group, cycloalkyl group, aryl group,aralkyl group, alkenyl group, etc., disclosed herein.

In particular aspects contemplated herein, D in formula (IIa) can be—N(CH₃)₂, —P(CH₃)₂, —N(CH₂CH₃)₂, —P(CH₂CH₃)₂, —N(Ph)₂, —P(Ph)₂, —OCH₃,—SCH₃, —OCH₂CH₃, —SCH₂CH₃, —OPh, or —SPh. For instance, D can be—N(CH₃)₂, —P(CH₃)₂, —N(CH₂CH₃)₂, —P(CH₂CH₃)₂, —N(Ph)₂, or —P(Ph)₂;alternatively, —OCH₃, —SCH₃, —OCH₂CH₃, —SCH₂CH₃, —OPh, or —SPh;alternatively, —N(CH₃)₂, —P(CH₃)₂, —N(CH₂CH₃)₂, —P(CH₂CH₃)₂;alternatively, —N(Ph)₂, or —P(Ph)₂; alternatively, —OCH₃, —SCH₃,—OCH₂CH₃, or —SCH₂CH₃; or alternatively, —OPh or —SPh.

In another embodiment of this invention, theN,N-bis[2-hydroxidebenzyl]amine compound can have the formula:

Within formula (IIb), M, X¹, X², L, D, R^(B1), R^(B2), R^(C1), andR^(C2) are independent elements of the N,N-bis[2-hydroxidebenzyl]aminecompound. Accordingly, the N,N-bis[2-hydroxidebenzyl]amine compoundhaving formula (IIb) can be described using any combination of M, X¹,X², L, D, R^(B1), R^(B2), R^(C1), and R^(C2) disclosed herein.

The selections for M, X¹, X², L, and D in formula (IIb) are the same asthose described herein above for formula (Ia). R^(B1), R^(B2), R^(C1),and R^(C2) independently can be a halide, C₁ to C₃₆ hydrocarbyl group,C₁ to C₃₆ halogenated hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group,or C₁ to C₃₆ hydrocarbylsilyl group, and these groups can be any halide,C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆ halogenated hydrocarbyl group, C₁to C₃₆ hydrocarboxy group, or C₁ to C₃₆ hydrocarbylsilyl group describedherein (e.g., as pertaining to R^(B) and R^(C) in formula (Ia)).

In one aspect, for example, R^(B1), R^(B2), R^(C1), and R^(C2)independently can be a methyl group, ethyl group, propyl group, butylgroup (e.g., t-Bu), pentyl group, hexyl group, propenyl group, butenylgroup, pentenyl group, hexenyl group, phenyl group, tolyl group, benzylgroup, trimethylsilyl group, triisopropylsilyl group, triphenylsilylgroup, allyldimethylsilyl group, CF₃, or Cl. In another aspect. R^(B1),R^(B2), R^(C1), and R^(C2) independently can be a methyl group, ethylgroup, propyl group, butyl group, pentyl group, hexyl group, propenylgroup, butenyl group, pentenyl group, hexenyl group, phenyl group, tolylgroup, or benzyl group. In yet another aspect, at least one of R^(B1),R^(B2), R^(C1), and R^(C2) (or alternatively, each of R^(B1), R^(B2),R^(C1), and R^(C2)) can be a methyl group; alternatively, an ethylgroup; alternatively, a propyl group; alternatively, a butyl group;alternatively, a pentyl group; alternatively, a hexyl group;alternatively, a propenyl group; alternatively, a butenyl group;alternatively, a pentenyl group; alternatively, a hexenyl group;alternatively, a phenyl group; alternatively, a tolyl group;alternatively, a benzyl group; alternatively, a trimethylsilyl group;alternatively, a triisopropylsilyl group; alternatively, atriphenylsilyl group; alternatively, an allyldimethylsilyl group;alternatively, CF₃; or alternatively, Cl. In these and other aspects, Lin formula (IIb) can be a C₁ to C₁₈ hydrocarbylene group, examples ofwhich can include, but are not limited to, a C₁ to C₄ alkylene group, aC₅ to C₈ cycloalkylene group, a C₆ to C₈ arylene group, a C₇ to C₈aralkylene group, and the like; and D can be a chemical group comprisingat least one of nitrogen, oxygen, phosphorus, and sulfur, examples ofwhich can include, but are not limited to, —N(CH₃)₂, —P(CH₃)₂,—N(CH₂CH₃)₂, —P(CH₂CH₃)₂, —N(Ph)₂, —P(Ph)₂, —OCH₃, —SCH₃, —OCH₂CH₃,—SCH₂CH₃, —OPh, —SPh, and the like.

Illustrative and non-limiting examples ofN,N-bis[2-hydroxidebenzyl]amine compounds having formula (IIa) andformula (IIb) can include, but are not limited to, compounds TM-A, TM-B,TM-C, and TM-D illustrated in FIG. 2.

Representative procedures for synthesizing compounds having formula(IIa) and formula (IIb) can be found in U.S. Pat. Nos. 6,333,423 and6,596,827, the disclosures of which are incorporated herein by referencein their entirety. Using analogous synthesis schemes, transition metalcomplexes similar to TM-A, TM-B, TM-C, and TM-D, but with monoanionicligands other than benzyl (e.g., halide, hydrocarbylaminyl,hydrocarbylsilyl, other hydrocarbyl, etc.), and/or with substituentsother than tert-butyl (e.g., halide, hydrocarboxy, hydrocarbylsilyl,other hydrocarbyl, etc.), and/or with different L and D groups, can bederived.

In another embodiment of this invention, theN,N-bis[2-hydroxidebenzyl]amine compound can have the formula:

Within formula (IIIa), M, X¹, X², R^(B), R^(C), p, q, and R^(E) areindependent elements of the N,N-bis[2-hydroxidebenzyl]amine compound.Accordingly, the N,N-bis[2-hydroxidebenzyl]amine compound having formula(IIIa) can be described using any combination of M, X¹, X², R^(B),R^(C), p, q, and R^(E) disclosed herein.

The selections for M, X¹, X², R^(B), R^(C), p, and q in formula (IIIa)are the same as those described herein above for formula (Ia). Forinstance, M can be Ti, Zr, or Hf; alternatively, M can be Ti;alternatively. M can be Zr, or alternatively, M can be Hf. X¹ and X² informula (IIIa) independently can be any monoanionic ligand disclosedherein, and this includes, but is not limited to, H, BH₄, a halide, a C₁to C₃₆ hydrocarbyl group, a C₁ to C₃₆ hydrocarboxy group, a C₁ to C₃₆hydrocarbylaminyl group, a C₁ to C₃₆ hydrocarbylsilyl group, a C₁ to C₃₆hydrocarbylaminylsilyl group, —OBR¹ ₂, or —OSO₂R¹, wherein R¹ is a C₁ toC₃₆ hydrocarbyl group. In some aspects, it is contemplated that X¹ andX² independently can be a C₁ to C₁₈ hydrocarbyl group, a C₁ to C₁₈hydrocarboxy group, a C₁ to C₁₈ hydrocarbylaminyl group, a C₁ to C₁₈hydrocarbylsilyl group, or a C₁ to C₁₈ hydrocarbylaminylsilyl group,while in other aspects, X¹ and X² independently can be a halide or a C₁to C₃₆ hydrocarbyl group. In formula (IIIa), each R^(B) and/or R^(C)independently can be any halide, C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆halogenated hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group, or C₁ toC₃₆ hydrocarbylsilyl group disclosed herein. For example, each R^(B)and/or R^(C) independently can be Cl, CF₃, a methyl group, an ethylgroup, a propyl group, a butyl group (e.g., t-Bu), a pentyl group, ahexyl group, a heptyl group, an octyl group, a nonyl group, a decylgroup, an ethenyl group, a propenyl group, a butenyl group, a pentenylgroup, a hexenyl group, a heptenyl group, an octenyl group, a nonenylgroup, a decenyl group, a phenyl group, a tolyl group, a benzyl group, anaphthyl group, a trimethylsilyl group, a triisopropylsilyl group, atriphenylsilyl group, or an allyldimethylsilyl group. The integers, pand q, independently can be 0, 1, 2, 3, or 4, such as, for instance, pcan be 0, 1, or 2, and q can be 0, 1, or 2.

R^(E) in formula (IIIa) can be any alkenyl group disclosed herein, forinstance, any C₂ to C₃₆ alkenyl group, any C₂ to C₁₈ alkenyl group, anyC₃ to C₁₂ alkenyl group, any C₃ to C₈ alkenyl group, or any C₃ to C₆alkenyl group disclosed herein. Accordingly, in one aspect, the alkenylgroup which can be RE in formula (IIIa) can be an ethenyl group, apropenyl group, a butenyl group, a pentenyl group, a hexenyl group, aheptenyl group, an octenyl group, a nonenyl group, a decenyl group, aundecenyl group, a dodecenyl group, a tridecenyl group, a tetradecenylgroup, a pentadecenyl group, a hexadecenyl group, a heptadecenyl group,or an octadecenyl group. In another aspect, R^(E) in formula (IIIa) canbe an ethenyl group, a propenyl group, a butenyl group, a pentenylgroup, a hexenyl group, a heptenyl group, an octenyl group, a nonenylgroup, or a decenyl group, while in yet another aspect, R^(E) in formula(IIIa) can be an ethenyl group, a propenyl group, a butenyl group, apentenyl group, or a hexenyl group. For example, R^(E) can be an ethenylgroup; alternatively, a propenyl group; alternatively, a butenyl group;alternatively, a pentenyl group; or alternatively, a hexenyl group. Instill another aspect, R^(E) can be a terminal alkenyl group, such as aC₃ to C₁₈ terminal alkenyl group, a C₃ to C₁₂ terminal alkenyl group, ora C₃ to C₈ terminal alkenyl group.

In another embodiment of this invention, theN,N-bis[2-hydroxidebenzyl]amine compound can have the formula:

Within formula (IIIb), M, X¹, X², R^(E), R^(B1), R^(B2), R^(C1), andR^(C2) are independent elements of the N,N-bis[2-hydroxidebenzyl]aminecompound. Accordingly, the N,N-bis[2-hydroxidebenzyl]amine compoundhaving formula (IIIb) can be described using any combination of M, X¹,X², R^(E), R^(B1), R^(B2), R^(C1), and R^(C2) disclosed herein.

The selections for M, X¹, X², and R^(E) in formula (IIIb) are the sameas those described herein above for formula (IIIa), while the selectionsfor R^(B1), R^(B2), R^(C1), and R^(C2) are the same as those describedherein above for formula (Ib). For example, M in formula (IIIb) can beTi, Zr, or Hf; X¹ and X² independently can be any monoanionic liganddisclosed herein; and R^(E) can be any alkenyl group disclosed herein(e.g., a propenyl group, a butenyl group, a pentenyl group, a hexenylgroup, a heptenyl group, an octenyl group, etc.). In these and otheraspects, R^(B1), R^(B2), R^(C1), and R^(C2) in formula (IIIb)independently can be any halide, C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆halogenated hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group, or C₁ toC₃₆ hydrocarbylsilyl group disclosed herein, examples of which caninclude, but are not limited to, Cl, CF₃, a methyl group, an ethylgroup, a propyl group, a butyl group (e.g., t-Bu), a pentyl group, ahexyl group, a heptyl group, an octyl group, a nonyl group, a decylgroup, an ethenyl group, a propenyl group, a butenyl group, a pentenylgroup, a hexenyl group, a heptenyl group, an octenyl group, a nonenylgroup, a decenyl group, a phenyl group, a tolyl group, a benzyl group, anaphthyl group, a trimethylsilyl group, a triisopropylsilyl group, atriphenylsilyl group, or an allyldimethylsilyl group, and the like.

Illustrative and non-limiting examples ofN,N-bis[2-hydroxidebenzyl]amine compounds having formula (IIIa) andformula (IIIb) can include, but are not limited to, compounds TM-1 andTM-2 illustrated in FIG. 1.

Methods of making transition metal complexes having formula (IIIa) andformula (IIIb) also are provided herein. Examples 1-8 that followprovide representative procedures for synthesizing compounds havingformula (IIIa) and formula (IIIb), or for synthesizing precursorcompounds useful in the subsequent synthesis of compounds having formula(IIIa) and formula (IIIb). Using analogous synthesis schemes to thoseprovided herein, transition metal complexes similar to TM-1 and TM-2,but with monoanionic ligands other than benzyl (e.g., halide,hydrocarbylaminyl, hydrocarbylsilyl, other hydrocarbyl, etc.), and/orwith substituents other than tert-butyl (e.g., halide, hydrocarboxy,hydrocarbylsilyl, other hydrocarbyl, etc.), and/or with a differentalkenyl group, can be derived.

Activator-Supports

The present invention encompasses various catalyst compositionscontaining an activator-support. In one embodiment, theactivator-support can comprise a chemically-treated solid oxide.Alternatively, in another embodiment, the activator-support can comprisea clay mineral, a pillared clay, an exfoliated clay, an exfoliated claygelled into another oxide matrix, a layered silicate mineral, anon-layered silicate mineral, a layered aluminosilicate mineral, anon-layered aluminosilicate mineral, or combinations thereof.

Generally, chemically-treated solid oxides exhibit enhanced acidity ascompared to the corresponding untreated solid oxide compound. Thechemically-treated solid oxide also can function as a catalyst activatoras compared to the corresponding untreated solid oxide. While thechemically-treated solid oxide can activate a transition metal complexin the absence of co-catalysts, it is not necessary to eliminateco-catalysts from the catalyst composition. The activation function ofthe activator-support can enhance the activity of catalyst compositionas a whole, as compared to a catalyst composition containing thecorresponding untreated solid oxide. However, it is believed that thechemically-treated solid oxide can function as an activator, even in theabsence of organoaluminum compounds, aluminoxanes, organoboron ororganoborate compounds, ionizing ionic compounds, and the like.

The chemically-treated solid oxide can comprise a solid oxide treatedwith an electron-withdrawing anion. While not intending to be bound bythe following statement, it is believed that treatment of the solidoxide with an electron-withdrawing component augments or enhances theacidity of the oxide. Thus, either the activator-support exhibits Lewisor Brønsted acidity that is typically greater than the Lewis or Brønstedacid strength of the untreated solid oxide, or the activator-support hasa greater number of acid sites than the untreated solid oxide, or both.One method to quantify the acidity of the chemically-treated anduntreated solid oxide materials can be by comparing the polymerizationactivities of the treated and untreated oxides under acid catalyzedreactions.

Chemically-treated solid oxides of this invention generally can beformed from an inorganic solid oxide that exhibits Lewis acidic orBrønsted acidic behavior and has a relatively high porosity. The solidoxide can be chemically-treated with an electron-withdrawing component,typically an electron-withdrawing anion, to form an activator-support.

According to one aspect of the present invention, the solid oxide usedto prepare the chemically-treated solid oxide can have a pore volumegreater than about 0.1 cc/g. According to another aspect of the presentinvention, the solid oxide can have a pore volume greater than about 0.5cc/g. According to yet another aspect of the present invention, thesolid oxide can have a pore volume greater than about 1.0 cc/g.

In another aspect, the solid oxide can have a surface area of from about100 to about 1000 m²/g. In yet another aspect, the solid oxide can havea surface area of from about 200 to about 800 m²/g. In still anotheraspect of the present invention, the solid oxide can have a surface areaof from about 250 to about 600 m²/g.

The chemically-treated solid oxide can comprise a solid inorganic oxidecomprising oxygen and one or more elements selected from Group 2, 3, 4,5, 6, 7, 8, 9, 10, 11, 12, 13, 14, or 15 of the periodic table, orcomprising oxygen and one or more elements selected from the lanthanideor actinide elements (See: Hawley's Condensed Chemical Dictionary.11^(th) Ed., John Wiley & Sons, 1995; Cotton, F. A., Wilkinson, G.,Murillo, C. A., and Bochmann, M., Advanced Inorganic Chemistry, 6^(th)Ed., Wiley-Interscience, 1999). For example, the inorganic oxide cancomprise oxygen and an element, or elements, selected from Al, B, Be,Bi, Cd, Co, Cr, Cu, Fe, Ga, La, Mn, Mo, Ni, Sb, Si, Sn, Sr, Th, Ti, V,W, P, Y, Zn, and Zr.

Suitable examples of solid oxide materials or compounds that can be usedto form the chemically-treated solid oxide can include, but are notlimited to, Al₂O₃, B₂O₃, BeO, Bi₂O₃, CdO, Co₃O₄, Cr₂O₃, CuO, Fe₂O₃,Ga₂O₃, La₂O₃, Mn₂O₃, MoO₃, NiO, P₂O₅, Sb₂O₅, SiO₂, SnO₂, SrO, ThO₂,TiO₂, V₂O₅, WO₃, Y₂O₃, ZnO, ZrO₂, and the like, including mixed oxidesthereof, and combinations thereof. For example, the solid oxide cancomprise silica, alumina, silica-alumina, silica-coated alumina,aluminum phosphate, aluminophosphate, heteropolytungstate, titania,zirconia, magnesia, boria, zinc oxide, mixed oxides thereof, or anycombination thereof.

The solid oxide of this invention encompasses oxide materials such asalumina, “mixed oxide” compounds thereof such as silica-alumina, andcombinations and mixtures thereof. The mixed oxide compounds such assilica-alumina can be single or multiple chemical phases with more thanone metal combined with oxygen to form a solid oxide compound. Examplesof mixed oxides that can be used in the activator-support of the presentinvention, either singly or in combination, can include, but are notlimited to, silica-alumina, silica-titania, silica-zirconia, zeolites,various clay minerals, alumina-titania, alumina-zirconia,zinc-aluminate, alumina-boria, silica-boria, aluminophosphate-silica,titania-zirconia, and the like. The solid oxide of this invention alsoencompasses oxide materials such as silica-coated alumina, as describedin U.S. Pat. No. 7,884,163, the disclosure of which is incorporatedherein by reference in its entirety.

The electron-withdrawing component used to treat the solid oxide can beany component that increases the Lewis or Brønsted acidity of the solidoxide upon treatment (as compared to the solid oxide that is not treatedwith at least one electron-withdrawing anion). According to one aspectof the present invention, the electron-withdrawing component can be anelectron-withdrawing anion derived from a salt, an acid, or othercompound, such as a volatile organic compound, that serves as a sourceor precursor for that anion. Examples of electron-withdrawing anions caninclude, but are not limited to, sulfate, bisulfate, fluoride, chloride,bromide, iodide, fluorosulfate, fluoroborate, phosphate,fluorophosphate, trifluoroacetate, triflate, fluorozirconate,fluorotitanate, phospho-tungstate, and the like, including mixtures andcombinations thereof. In addition, other ionic or non-ionic compoundsthat serve as sources for these electron-withdrawing anions also can beemployed in the present invention. It is contemplated that theelectron-withdrawing anion can be, or can comprise, fluoride, chloride,bromide, phosphate, triflate, bisulfate, or sulfate, and the like, orany combination thereof, in some aspects of this invention. In otheraspects, the electron-withdrawing anion can comprise sulfate, bisulfate,fluoride, chloride, bromide, iodide, fluorosulfate, fluoroborate,phosphate, fluorophosphate, trifluoroacetate, triflate, fluorozirconate,fluorotitanate, and the like, or combinations thereof.

Thus, for example, the activator-support (e.g., chemically-treated solidoxide) used in the catalyst compositions of the present invention canbe, or can comprise, fluorided alumina, chlorided alumina, bromidedalumina, sulfated alumina, fluorided silica-alumina, chloridedsilica-alumina, bromided silica-alumina, sulfated silica-alumina,fluorided silica-zirconia, chlorided silica-zirconia, bromidedsilica-zirconia, sulfated silica-zirconia, fluorided silica-titania,fluorided silica-coated alumina, sulfated silica-coated alumina,phosphated silica-coated alumina, and the like, or combinations thereof.In one aspect, the activator-support can be, or can comprise, fluoridedalumina, sulfated alumina, fluorided silica-alumina, sulfatedsilica-alumina, fluorided silica-coated alumina, sulfated silica-coatedalumina, phosphated silica-coated alumina, and the like, or anycombination thereof. In another aspect, the activator-support cancomprise fluorided alumina; alternatively, chlorided alumina;alternatively, sulfated alumina; alternatively, fluoridedsilica-alumina; alternatively, sulfated silica-alumina; alternatively,fluorided silica-zirconia; alternatively, chlorided silica-zirconia; oralternatively, fluorided silica-coated alumina.

When the electron-withdrawing component comprises a salt of anelectron-withdrawing anion, the counterion or cation of that salt can beselected from any cation that allows the salt to revert or decomposeback to the acid during calcining. Factors that dictate the suitabilityof the particular salt to serve as a source for the electron-withdrawinganion can include, but are not limited to, the solubility of the salt inthe desired solvent, the lack of adverse reactivity of the cation,ion-pairing effects between the cation and anion, hygroscopic propertiesimparted to the salt by the cation, and the like, and thermal stabilityof the anion. Examples of suitable cations in the salt of theelectron-withdrawing anion can include, but are not limited to,ammonium, trialkyl ammonium, tetraalkyl ammonium, tetraalkylphosphonium, H⁺, [H(OEt₂)₂]⁺, and the like.

Further, combinations of one or more different electron-withdrawinganions, in varying proportions, can be used to tailor the specificacidity of the activator-support to the desired level. Combinations ofelectron-withdrawing components can be contacted with the oxide materialsimultaneously or individually, and in any order that affords thedesired chemically-treated solid oxide acidity. For example, one aspectof this invention can employ two or more electron-withdrawing anionsource compounds in two or more separate contacting steps.

Thus, a process by which a chemically-treated solid oxide can beprepared is as follows: a selected solid oxide, or combination of solidoxides, can be contacted with a first electron-withdrawing anion sourcecompound to form a first mixture; this first mixture can be calcined andthen contacted with a second electron-withdrawing anion source compoundto form a second mixture; the second mixture then can be calcined toform a treated solid oxide. In such a process, the first and secondelectron-withdrawing anion source compounds can be either the same ordifferent compounds.

According to another aspect of the present invention, thechemically-treated solid oxide can comprise a solid inorganic oxidematerial, a mixed oxide material, or a combination of inorganic oxidematerials, that is chemically-treated with an electron-withdrawingcomponent, and optionally treated with a metal source, including metalsalts, metal ions, or other metal-containing compounds. Non-limitingexamples of the metal or metal ion can include zinc, nickel, vanadium,titanium, silver, copper, gallium, tin, tungsten, molybdenum, zirconium,and the like, or combinations thereof. Examples of chemically-treatedsolid oxides that contain a metal or metal ion can include, but are notlimited to, chlorided zinc-impregnated alumina, fluoridedtitanium-impregnated alumina, fluorided zinc-impregnated alumina,chlorided zinc-impregnated silica-alumina, fluorided zinc-impregnatedsilica-alumina, sulfated zinc-impregnated alumina, chlorided zincaluminate, fluorided zinc aluminate, sulfated zinc aluminate,silica-coated alumina treated with hexafluorotitanic acid, silica-coatedalumina treated with zinc and then fluorided, and the like, or anycombination thereof.

Any method of impregnating the solid oxide material with a metal can beused. The method by which the oxide is contacted with a metal source,typically a salt or metal-containing compound, can include, but is notlimited to, gelling, co-gelling, impregnation of one compound ontoanother, and the like. If desired, the metal-containing compound can beadded to or impregnated into the solid oxide in solution form, andsubsequently converted into the supported metal upon calcining.Accordingly, the solid inorganic oxide can further comprise a metalselected from zinc, titanium, nickel, vanadium, silver, copper, gallium,tin, tungsten, molybdenum, and the like, or combinations of thesemetals. For example, zinc often can be used to impregnate the solidoxide because it can provide improved catalyst activity at a low cost.

The solid oxide can be treated with metal salts or metal-containingcompounds before, after, or at the same time that the solid oxide istreated with the electron-withdrawing anion. Following any contactingmethod, the contacted mixture of solid compound, electron-withdrawinganion, and the metal ion can be calcined. Alternatively, a solid oxidematerial, an electron-withdrawing anion source, and the metal salt ormetal-containing compound can be contacted and calcined simultaneously.

Various processes can be used to form the chemically-treated solid oxideuseful in the present invention. The chemically-treated solid oxide cancomprise the contact product of one or more solid oxides with one ormore electron-withdrawing anion sources. It is not required that thesolid oxide be calcined prior to contacting the electron-withdrawinganion source. Typically, the contact product can be calcined eitherduring or after the solid oxide is contacted with theelectron-withdrawing anion source. The solid oxide can be calcined oruncalcined. Various processes to prepare solid oxide activator-supportsthat can be employed in this invention have been reported. For example,such methods are described in U.S. Pat. Nos. 6,107,230, 6,165,929,6,294,494, 6,300,271, 6,316,553, 6,355,594, 6,376,415, 6,388,017,6,391,816, 6,395,666, 6,524,987, 6,548,441, 6,548,442, 6,576,583,6,613,712, 6,632,894, 6,667,274, and 6,750,302, the disclosures of whichare incorporated herein by reference in their entirety.

According to one aspect of the present invention, the solid oxidematerial can be chemically-treated by contacting it with anelectron-withdrawing component, typically an electron-withdrawing anionsource. Further, the solid oxide material optionally can be chemicallytreated with a metal ion, and then calcined to form a metal-containingor metal-impregnated chemically-treated solid oxide. According toanother aspect of the present invention, the solid oxide material andelectron-withdrawing anion source can be contacted and calcinedsimultaneously.

The method by which the oxide is contacted with the electron-withdrawingcomponent, typically a salt or an acid of an electron-withdrawing anion,can include, but is not limited to, gelling, co-gelling, impregnation ofone compound onto another, and the like. Thus, following any contactingmethod, the contacted mixture of the solid oxide, electron-withdrawinganion, and optional metal ion, can be calcined.

The solid oxide activator-support (i.e., chemically-treated solid oxide)thus can be produced by a process comprising:

1) contacting a solid oxide (or solid oxides) with anelectron-withdrawing anion source compound (or compounds) to form afirst mixture; and

2) calcining the first mixture to form the solid oxideactivator-support.

According to another aspect of the present invention, the solid oxideactivator-support (chemically-treated solid oxide) can be produced by aprocess comprising:

1) contacting a solid oxide (or solid oxides) with a firstelectron-withdrawing anion source compound to form a first mixture;

2) calcining the first mixture to produce a calcined first mixture;

3) contacting the calcined first mixture with a secondelectron-withdrawing anion source compound to form a second mixture; and

4) calcining the second mixture to form the solid oxideactivator-support.

According to yet another aspect of the present invention, thechemically-treated solid oxide can be produced or formed by contactingthe solid oxide with the electron-withdrawing anion source compound,where the solid oxide compound is calcined before, during, or aftercontacting the electron-withdrawing anion source, and where there is asubstantial absence of aluminoxanes, organoboron or organoboratecompounds, and ionizing ionic compounds.

Calcining of the treated solid oxide generally can be conducted in anambient atmosphere, typically in a dry ambient atmosphere, at atemperature from about 200° C. to about 900° C., and for a time of about1 minute to about 100 hours. Calcining can be conducted at a temperatureof from about 300° C. to about 800° C., or alternatively, at atemperature of from about 400° C. to about 700° C. Calcining can beconducted for about 30 minutes to about 50 hours, or for about 1 hour toabout 15 hours. Thus, for example, calcining can be carried out forabout 1 to about 10 hours at a temperature of from about 350° C. toabout 550° C. Any suitable ambient atmosphere can be employed duringcalcining. Generally, calcining can be conducted in an oxidizingatmosphere, such as air. Alternatively, an inert atmosphere, such asnitrogen or argon, or a reducing atmosphere, such as hydrogen or carbonmonoxide, can be used.

According to one aspect of the present invention, the solid oxidematerial can be treated with a source of halide ion, sulfate ion, or acombination of anions, optionally treated with a metal ion, and thencalcined to provide the chemically-treated solid oxide in the form of aparticulate solid. For example, the solid oxide material can be treatedwith a source of sulfate (termed a “sulfating agent”), a source ofbromide ion (termed a “bromiding agent”), a source of chloride ion(termed a “chloriding agent”), a source of fluoride ion (termed a“fluoriding agent”), or a combination thereof, and calcined to providethe solid oxide activator. Useful acidic activator-supports can include,but are not limited to, bromided alumina, chlorided alumina, fluoridedalumina, sulfated alumina, bromided silica-alumina, chloridedsilica-alumina, fluorided silica-alumina, sulfated silica-alumina,bromided silica-zirconia, chlorided silica-zirconia, fluoridedsilica-zirconia, sulfated silica-zirconia, fluorided silica-titania,alumina treated with hexafluorotitanic acid, silica-coated aluminatreated with hexafluorotitanic acid, silica-alumina treated withhexafluorozirconic acid, silica-alumina treated with trifluoroaceticacid, fluorided boria-alumina, silica treated with tetrafluoroboricacid, alumina treated with tetrafluoroboric acid, alumina treated withhexafluorophosphoric acid, a pillared clay, such as a pillaredmontmorillonite, optionally treated with fluoride, chloride, or sulfate;phosphated alumina or other aluminophosphates optionally treated withsulfate, fluoride, or chloride; or any combination of the above.Further, any of these activator-supports optionally can be treated orimpregnated with a metal ion.

The chemically-treated solid oxide can comprise a fluorided solid oxidein the form of a particulate solid. The fluorided solid oxide can beformed by contacting a solid oxide with a fluoriding agent. The fluorideion can be added to the oxide by forming a slurry of the oxide in asuitable solvent such as alcohol or water including, but not limited to,the one to three carbon alcohols because of their volatility and lowsurface tension. Examples of suitable fluoriding agents can include, butare not limited to, hydrofluoric acid (HF), ammonium fluoride (NH₄F),ammonium bifluoride (NH₄HF₂), ammonium tetrafluoroborate (NH₄BF₄),ammonium silicofluoride (hexafluorosilicate) ((NH₄)₂SiF₆), ammoniumhexafluorophosphate (NH₄PF₆), hexafluorotitanic acid (H₂TiF₆), ammoniumhexafluorotitanic acid ((NH₄)₂TiF₆), hexafluorozirconic acid (H₂ZrF₆),AlF₃, NH₄AlF₄, analogs thereof, and combinations thereof. Triflic acidand ammonium triflate also can be employed. For example, ammoniumbifluoride (NH₄HF₂) can be used as the fluoriding agent, due to its easeof use and availability.

If desired, the solid oxide can be treated with a fluoriding agentduring the calcining step. Any fluoriding agent capable of thoroughlycontacting the solid oxide during the calcining step can be used. Forexample, in addition to those fluoriding agents described previously,volatile organic fluoriding agents can be used. Examples of volatileorganic fluoriding agents useful in this aspect of the invention caninclude, but are not limited to, freons, perfluorohexane,perfluorobenzene, fluoromethane, trifluoroethanol, and the like, andcombinations thereof. Calcining temperatures generally must be highenough to decompose the compound and release fluoride. Gaseous hydrogenfluoride (HF) or fluorine (F₂) itself also can be used with the solidoxide if fluorided while calcining. Silicon tetrafluoride (SiF₄) andcompounds containing tetrafluoroborate (BF₄ ⁻) also can be employed. Oneconvenient method of contacting the solid oxide with the fluoridingagent can be to vaporize a fluoriding agent into a gas stream used tofluidize the solid oxide during calcination.

Similarly, in another aspect of this invention, the chemically-treatedsolid oxide can comprise a chlorided solid oxide in the form of aparticulate solid. The chlorided solid oxide can be formed by contactinga solid oxide with a chloriding agent. The chloride ion can be added tothe oxide by forming a slurry of the oxide in a suitable solvent. Thesolid oxide can be treated with a chloriding agent during the calciningstep. Any chloriding agent capable of serving as a source of chlorideand thoroughly contacting the oxide during the calcining step can beused, such as SiCl₄, SiMe₂Cl₂, TiCl₄, BCl₃, and the like, includingmixtures thereof. Volatile organic chloriding agents can be used.Examples of suitable volatile organic chloriding agents can include, butare not limited to, certain freons, perchlorobenzene, chloromethane,dichloromethane, chloroform, carbon tetrachloride, trichloroethanol, andthe like, or any combination thereof. Gaseous hydrogen chloride orchlorine itself also can be used with the solid oxide during calcining.One convenient method of contacting the oxide with the chloriding agentcan be to vaporize a chloriding agent into a gas stream used to fluidizethe solid oxide during calcination.

The amount of fluoride or chloride ion present before calcining thesolid oxide generally can be from about 1 to about 50% by weight, wherethe weight percent is based on the weight of the solid oxide, forexample, silica-alumina, before calcining. According to another aspectof this invention, the amount of fluoride or chloride ion present beforecalcining the solid oxide can be from about 1 to about 25% by weight,and according to another aspect of this invention, from about 2 to about20% by weight. According to yet another aspect of this invention, theamount of fluoride or chloride ion present before calcining the solidoxide can be from about 4 to about 10% by weight. Once impregnated withhalide, the halided oxide can be dried by any suitable method including,but not limited to, suction filtration followed by evaporation, dryingunder vacuum, spray drying, and the like, although it is also possibleto initiate the calcining step immediately without drying theimpregnated solid oxide.

The silica-alumina used to prepare the treated silica-alumina typicallycan have a pore volume greater than about 0.5 cc/g. According to oneaspect of the present invention, the pore volume can be greater thanabout 0.8 cc/g, and according to another aspect of the presentinvention, greater than about 1.0 cc/g. Further, the silica-aluminagenerally can have a surface area greater than about 100 m²/g. Accordingto another aspect of this invention, the surface area can be greaterthan about 250 m/g. Yet, in another aspect, the surface area can begreater than about 350 m²/g.

The silica-alumina utilized in the present invention typically can havean alumina content from about 5 to about 95% by weight. According to oneaspect of this invention, the alumina content of the silica-alumina canbe from about 5 to about 50%, or from about 8% to about 30%, alumina byweight. In another aspect, high alumina content silica-alumina compoundscan be employed, in which the alumina content of these silica-aluminacompounds typically ranges from about 60% to about 90%, or from about65% to about 80%, alumina by weight. According to yet another aspect ofthis invention, the solid oxide component can comprise alumina withoutsilica, and according to another aspect of this invention, the solidoxide component can comprise silica without alumina.

The sulfated solid oxide can comprise sulfate and a solid oxidecomponent, such as alumina or silica-alumina, in the form of aparticulate solid. Optionally, the sulfated oxide can be treated furtherwith a metal ion such that the calcined sulfated oxide comprises ametal. According to one aspect of the present invention, the sulfatedsolid oxide can comprise sulfate and alumina. In some instances, thesulfated alumina can be formed by a process wherein the alumina istreated with a sulfate source, for example, sulfuric acid or a sulfatesalt such as ammonium sulfate. This process generally can be performedby forming a slurry of the alumina in a suitable solvent, such asalcohol or water, in which the desired concentration of the sulfatingagent has been added. Suitable organic solvents can include, but are notlimited to, the one to three carbon alcohols because of their volatilityand low surface tension.

According to one aspect of this invention, the amount of sulfate ionpresent before calcining can be from about 0.5 to about 100 parts byweight sulfate ion to about 100 parts by weight solid oxide. Accordingto another aspect of this invention, the amount of sulfate ion presentbefore calcining can be from about 1 to about 50 parts by weight sulfateion to about 100 parts by weight solid oxide, and according to stillanother aspect of this invention, from about 5 to about 30 parts byweight sulfate ion to about 100 parts by weight solid oxide. Theseweight ratios are based on the weight of the solid oxide beforecalcining. Once impregnated with sulfate, the sulfated oxide can bedried by any suitable method including, but not limited to, suctionfiltration followed by evaporation, drying under vacuum, spray drying,and the like, although it is also possible to initiate the calciningstep immediately.

According to another aspect of the present invention, theactivator-support used in preparing the catalyst compositions of thisinvention can comprise an ion-exchangeable activator-support including,but not limited to, silicate and aluminosilicate compounds or minerals,either with layered or non-layered structures, and combinations thereof.In another aspect of this invention, ion-exchangeable, layeredaluminosilicates such as pillared clays can be used asactivator-supports. When the acidic activator-support comprises anion-exchangeable activator-support, it can optionally be treated with atleast one electron-withdrawing anion such as those disclosed herein,though typically the ion-exchangeable activator-support is not treatedwith an electron-withdrawing anion.

According to another aspect of the present invention, theactivator-support of this invention can comprise clay minerals havingexchangeable cations and layers capable of expanding. Typical claymineral activator-supports can include, but are not limited to,ion-exchangeable, layered aluminosilicates such as pillared clays.Although the term “support” is used, it is not meant to be construed asan inert component of the catalyst composition, but rather can beconsidered an active part of the catalyst composition, because of itsintimate association with the transition metal complex component.

According to another aspect of the present invention, the clay materialsof this invention can encompass materials either in their natural stateor that have been treated with various ions by wetting, ion exchange, orpillaring. Typically, the clay material activator-support of thisinvention can comprise clays that have been ion exchanged with largecations, including polynuclear, highly charged metal complex cations.However, the clay material activator-supports of this invention also canencompass clays that have been ion exchanged with simple salts,including, but not limited to, salts of Al(III), Fe(II), Fe(III), andZn(II) with ligands such as halide, acetate, sulfate, nitrate, ornitrite.

According to another aspect of the present invention, theactivator-support can comprise a pillared clay. The term “pillared clay”is used to refer to clay materials that have been ion exchanged withlarge, typically polynuclear, highly charged metal complex cations.Examples of such ions can include, but are not limited to, Keggin ionswhich can have charges such as 7+, various polyoxometallates, and otherlarge ions. Thus, the term pillaring can refer to a simple exchangereaction in which the exchangeable cations of a clay material arereplaced with large, highly charged ions, such as Keggin ions. Thesepolymeric cations then can be immobilized within the interlayers of theclay and when calcined are converted to metal oxide “pillars,”effectively supporting the clay layers as column-like structures. Thus,once the clay is dried and calcined to produce the supporting pillarsbetween clay layers, the expanded lattice structure can be maintainedand the porosity can be enhanced. The resulting pores can vary in shapeand size as a function of the pillaring material and the parent claymaterial used. Examples of pillaring and pillared clays are found in: T.J. Pinnavaia, Science 220 (4595), 365-371 (1983); J. M. Thomas,Intercalation Chemistry, (S. Whittington and A. Jacobson, eds.) Ch. 3,pp. 55-99, Academic Press, Inc., (1972); U.S. Pat. Nos. 4,452,910 ;5,376,611; and 4,060,480; the disclosures of which are incorporatedherein by reference in their entirety.

The pillaring process can utilize clay minerals having exchangeablecations and layers capable of expanding. Any pillared clay that canenhance the polymerization of olefins in the catalyst composition of thepresent invention can be used. Therefore, suitable clay minerals forpillaring can include, but are not limited to, allophanes; smectites,both dioctahedral (Al) and tri-octahedral (Mg) and derivatives thereofsuch as montmorillonites (bentonites), nontronites, hectorites, orlaponites; halloysites; vermiculites; micas; fluoromicas; chlorites;mixed-layer clays; the fibrous clays including but not limited tosepiolites, attapulgites, and palygorskites; a serpentine clay; illite;laponite; saponite; and any combination thereof. In one aspect, thepillared clay activator-support can comprise bentonite ormontmorillonite. The principal component of bentonite ismontmorillonite.

The pillared clay can be pretreated if desired. For example, a pillaredbentonite can be pretreated by drying at about 300° C. under an inertatmosphere, typically dry nitrogen, for about 3 hours, before beingadded to the polymerization reactor. Although an exemplary pretreatmentis described herein, it should be understood that the preheating can becarried out at many other temperatures and times, including anycombination of temperature and time steps, all of which are encompassedby this invention.

The activator-support used to prepare the catalyst compositions of thepresent invention can be combined with other inorganic supportmaterials, including, but not limited to, zeolites, inorganic oxides,phosphated inorganic oxides, and the like. In one aspect, typicalsupport materials that can be used include, but are not limited to,silica, silica-alumina, alumina, titania, zirconia, magnesia, boria,thoria, aluminophosphate, aluminum phosphate, silica-titania,coprecipitated silica/titania, mixtures thereof, or any combinationthereof.

According to another aspect of the present invention, one or more of thetransition metal complexes can be precontacted with an olefin monomerand an organoaluminum compound for a first period of time prior tocontacting this mixture with the activator-support. Once theprecontacted mixture of the transition metal complex(es), olefinmonomer, and organoaluminum compound is contacted with theactivator-support, the composition further comprising theactivator-support can be termed a “postcontacted” mixture. Thepostcontacted mixture can be allowed to remain in further contact for asecond period of time prior to being charged into the reactor in whichthe polymerization process will be carried out.

According to yet another aspect of the present invention, one or more ofthe transition metal complexes can be precontacted with an olefinmonomer and an activator-support for a first period of time prior tocontacting this mixture with the organoaluminum compound. Once theprecontacted mixture of the transition metal complex(es), olefinmonomer, and activator-support is contacted with the organoaluminumcompound, the composition further comprising the organoalumninum can betermed a “postcontacted” mixture. The postcontacted mixture can beallowed to remain in further contact for a second period of time priorto being introduced into the polymerization reactor.

Co-Catalysts

In certain embodiments directed to catalyst compositions containing aco-catalyst, the co-catalyst can comprise a metal hydrocarbyl compound,examples of which include non-halide metal hydrocarbyl compounds, metalhydrocarbyl halide compounds, non-halide metal alkyl compounds, metalalkyl halide compounds, and so forth. The hydrocarbyl group (or alkylgroup) can be any hydrocarbyl (or alkyl) group disclosed herein.Moreover, in some aspects, the metal of the metal hydrocarbyl can be agroup 1, 2, 11, 12, 13, or 14 metal; alternatively, a group 13 or 14metal; or alternatively, a group 13 metal. Hence, in some aspects, themetal of the metal hydrocarbyl (non-halide metal hydrocarbyl or metalhydrocarbyl halide) can be lithium, sodium, potassium, rubidium, cesium,beryllium, magnesium, calcium, strontium, barium, zinc, cadmium, boron,aluminum, or tin; alternatively, lithium, sodium, potassium, magnesium,calcium, zinc, boron, aluminum, or tin; alternatively, lithium, sodium,or potassium; alternatively, magnesium or calcium; alternatively,lithium; alternatively, sodium; alternatively, potassium; alternatively,magnesium; alternatively, calcium; alternatively, zinc; alternatively,boron; alternatively, aluminum; or alternatively, tin. In some aspects,the metal hydrocarbyl or metal alkyl, with or without a halide, cancomprise a lithium hydrocarbyl or alkyl, a magnesium hydrocarbyl oralkyl, a boron hydrocarbyl or alkyl, a zinc hydrocarbyl or alkyl, or analuminum hydrocarbyl or alkyl.

In particular embodiments directed to catalyst compositions containing aco-catalyst, the co-catalyst can comprise an aluminoxane compound, anorganoboron or organoborate compound, an ionizing ionic compound, anorganoaluminum compound, an organozinc compound, an organomagnesiumcompound, or an organolithium compound, and this includes anycombinations of these materials. In one aspect, the co-catalyst cancomprise an organoaluminum compound. In another aspect, the co-catalystcan comprise an aluminoxane compound, an organoboron or organoboratecompound, an ionizing ionic compound, an organozinc compound, anorganomagnesium compound, an organolithium compound, or any combinationthereof. In yet another aspect, the co-catalyst can comprise analuminoxane compound; alternatively, an organoboron or organoboratecompound; alternatively, an ionizing ionic compound; alternatively, anorganozinc compound; alternatively, an organomagnesium compound; oralternatively, an organolithium compound.

Organoaluminum Compounds

In some embodiments, catalyst compositions of the present invention cancomprise one or more organoaluminum compounds. Such compounds caninclude, but are not limited to, compounds having the formula:(R^(X))₃Al;where each R^(X) independently can be an aliphatic group having from 1to 10 carbon atoms. For example, each R^(X) independently can be methyl,ethyl, propyl, butyl, hexyl, or isobutyl.

Other organoaluminum compounds which can be used in catalystcompositions disclosed herein can include, but are not limited to,compounds having the formula:Al(X⁵)_(m)(X⁶)_(3-m),where each X⁵ independently can be a hydrocarbyl; each X⁶ independentlycan be an alkoxide or an aryloxide, a halide, or a hydride; and m can befrom 1 to 3, inclusive. Hydrocarbyl is used herein to specify ahydrocarbon radical group and includes, for instance, aryl, alkyl,cycloalkyl, alkenyl, cycloalkenyl, cycloalkadienyl, alkynyl, aralkyl,aralkenyl, and aralkynyl groups.

In one aspect, each X⁵ independently can be a hydrocarbyl having from 1to about 18 carbon atoms. In another aspect of the present invention,each X⁵ independently can be an alkyl having from 1 to 10 carbon atoms.For example, each X⁵ independently can be methyl, ethyl, propyl,n-butyl, sec-butyl, isobutyl, or hexyl, and the like, in yet anotheraspect of the present invention.

According to one aspect of the present invention, each X independentlycan be an alkoxide or an aryloxide, any one of which has from 1 to 18carbon atoms, a halide, or a hydride. In another aspect of the presentinvention, each X⁶ can be selected independently from fluorine andchlorine. Yet, in another aspect, X⁶ can be chlorine.

In the formula, Al(X⁵)_(m)(X⁶)_(3-m), m can be a number from 1 to 3,inclusive, and typically, m can be 3. The value of m is not restrictedto be an integer; therefore, this formula can include sesquihalidecompounds or other organoaluminum cluster compounds.

Examples of organoaluminum compounds suitable for use in accordance withthe present invention can include, but are not limited to,trialkylaluminum compounds, dialkylaluminum halide compounds,dialkylaluminum alkoxide compounds, dialkylaluminum hydride compounds,and combinations thereof. Specific non-limiting examples of suitableorganoaluminum compounds can include trimethylaluminum (TMA),triethylaluminum (TEA), tri-n-propylaluminum (TNPA), tri-n-butylaluminum(TNBA), triisobutylaluminum (TIBA), tri-n-hexylaluminum,tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminumethoxide, diethylaluminum chloride, and the like, or combinationsthereof.

The present invention contemplates a method of precontacting atransition metal complex with an organoaluminum compound and an olefinmonomer to form a precontacted mixture, prior to contacting thisprecontacted mixture with an activator-support to form a catalystcomposition. When the catalyst composition is prepared in this manner,typically, though not necessarily, a portion of the organoaluminumcompound can be added to the precontacted mixture and another portion ofthe organoaluminum compound can be added to the postcontacted mixtureprepared when the precontacted mixture is contacted with the solid oxideactivator-support. However, the entire organoaluminum compound can beused to prepare the catalyst composition in either the precontacting orpostcontacting step. Alternatively, all the catalyst components can becontacted in a single step.

Further, more than one organoaluminum compound can be used in either theprecontacting or the postcontacting step. When an organoaluminumcompound is added in multiple steps, the amounts of organoaluminumcompound disclosed herein include the total amount of organoaluminumcompound used in both the precontacted and postcontacted mixtures, andany additional organoaluminum compound added to the polymerizationreactor. Therefore, total amounts of organoaluminum compounds aredisclosed regardless of whether a single organoaluminum compound or morethan one organoaluminum compound is used.

Aluminoxane Compounds

Certain embodiments of the present invention provide a catalystcomposition which can comprise an aluminoxane compound. As used herein,the term “aluminoxane” refers to aluminoxane compounds, compositions,mixtures, or discrete species, regardless of how such aluminoxanes areprepared, formed or otherwise provided. For example, a catalystcomposition comprising an aluminoxane compound can be prepared in whichaluminoxane is provided as the poly(hydrocarbyl aluminum oxide), or inwhich aluminoxane is provided as the combination of an aluminum alkylcompound and a source of active protons such as water. Aluminoxanes alsocan be referred to as poly(hydrocarbyl aluminum oxides) ororganoaluminoxanes.

The other catalyst components typically can be contacted with thealuminoxane in a saturated hydrocarbon compound solvent, though anysolvent that is substantially inert to the reactants, intermediates, andproducts of the activation step can be used. The catalyst compositionformed in this manner can be collected by any suitable method, forexample, by filtration. Alternatively, the catalyst composition can beintroduced into the polymerization reactor without being isolated.

The aluminoxane compound of this invention can be an oligomeric aluminumcompound comprising linear structures, cyclic structures, or cagestructures, or mixtures of all three. Cyclic aluminoxane compoundshaving the formula:

wherein each R in this formula independently can be a linear or branchedalkyl having from 1 to 10 carbon atoms, and p in this formula can be aninteger from 3 to 20, are encompassed by this invention. The AlRO moietyshown here also can constitute the repeating unit in a linearaluminoxane. Thus linear aluminoxanes having the formula:

wherein each R in this formula independently can be a linear or branchedalkyl having from 1 to 10 carbon atoms, and q in this formula can be aninteger from 1 to 50, are also encompassed by this invention.

Further, aluminoxanes can have cage structures of the formula R^(t)_(5r+α)R^(b) _(r-α)Al_(4r)O_(3r), wherein each R^(t) independently canbe a terminal linear or branched alkyl group having from 1 to 10 carbonatoms; each R^(b) independently can be a bridging linear or branchedalkyl group having from 1 to 10 carbon atoms; r can be 3 or 4; and α canbe equal to n_(Al(3))−n_(O(2))+n_(O(4)), wherein n_(Al(3)) is the numberof three coordinate aluminum atoms, n_(O(2)) is the number of twocoordinate oxygen atoms, and n_(O(4)) is the number of 4 coordinateoxygen atoms.

Thus, aluminoxanes which can be employed in the catalyst compositions ofthe present invention can be represented generally by formulas such as(R—Al—O)_(p), R(R—Al—O)_(q)AlR₂, and the like. In these formulas, each Rgroup independently can be a linear or branched C₁-C₆ alkyl, such asmethyl, ethyl propyl, butyl, pentyl, or hexyl. Examples of aluminoxanecompounds that can be used in accordance with the present invention caninclude, but are not limited to, methylaluminoxane, modifiedmethylaluminoxane, ethylaluminoxane, n-propylaluminoxane,iso-propylaluminoxane, n-butylaluminoxane, t-butylaluminoxane,sec-butylaluminoxane, iso-butylaluminoxane, 1-pentylaluminoxane,2-pentylaluminoxane, 3-pentylaluminoxane, isopentylaluminoxane,neopentylaluminoxane, and the like, or any combination thereof.Methylaluminoxane, ethylaluminoxane, and iso-butylaluminoxane can beprepared from trimethylaluminum, triethylaluminum, ortriisobutylaluminum, respectively, and sometimes are referred to aspoly(methyl aluminum oxide), poly(ethyl aluminum oxide), andpoly(isobutyl aluminum oxide), respectively. It is also within the scopeof the invention to use an aluminoxane in combination with atrialkylaluminum, such as that disclosed in U.S. Pat. No. 4,794,096,incorporated herein by reference in its entirety.

The present invention contemplates many values of p and q in thealuminoxane formulas (R—Al—O)_(p) and R(R—Al—O)_(q)AlR₂, respectively.In some aspects, p and q can be at least 3. However, depending upon howthe organoaluminoxane is prepared, stored, and used, the value of p andq can vary within a single sample of aluminoxane, and such combinationsof organoaluminoxanes are contemplated herein.

In preparing a catalyst composition containing an aluminoxane, the molarratio of the total moles of aluminum in the aluminoxane (oraluminoxanes) to the total moles of transition metal complex(es) in thecomposition generally can be between about 1:10 and about 100,000:1. Inanother aspect, the molar ratio can be in a range from about 5:1 toabout 15,000:1. Optionally, aluminoxane can be added to a polymerizationzone in ranges from about 0.01 mg/L to about 1000 mg/L, from about 0.1mg/L to about 100 mg/L, or from about 1 mg/L to about 50 mg/L.

Organoaluminoxanes can be prepared by various procedures. Examples oforganoaluminoxane preparations are disclosed in U.S. Pat. Nos. 3,242,099and 4,808,561, the disclosures of which are incorporated herein byreference in their entirety. For example, water in an inert organicsolvent can be reacted with an aluminum alkyl compound, such as(R^(X))₃Al, to form the desired organoaluminoxane compound. While notintending to be bound by this statement, it is believed that thissynthetic method can afford a mixture of both linear and cyclic R—Al—Oaluminoxane species, both of which are encompassed by this invention.Alternatively, organoaluminoxanes can be prepared by reacting analuminum alkyl compound, such as (R^(X))₃Al, with a hydrated salt, suchas hydrated copper sulfate, in an inert organic solvent.

Organoboron & Organoborate Compounds

According to another embodiment of the present invention, the catalystcomposition can comprise an organoboron or organoborate compound. Suchcompounds can include neutral boron compounds, borate salts, and thelike, or combinations thereof. For example, fluoroorgano boron compoundsand fluoroorgano borate compounds are contemplated.

Any fluoroorgano boron or fluoroorgano borate compound can be utilizedwith the present invention. Examples of fluoroorgano borate compoundsthat can be used in the present invention can include, but are notlimited to, fluorinated aryl borates such as N,N-dimethylaniliniumtetrakis(pentafluorophenyl)borate, triphenylcarbeniumtetrakis(pentafluorophenyl)borate, lithiumtetrakis(pentafluorophenyl)borate, N,N-dimethylaniliniumtetrakis[3,5-bis(trifluoromethyl)phenyl]borate, triphenylcarbeniumtetrakis[3,5-bis(trifluoromethyl)phenyl]borate, and the like, ormixtures thereof. Examples of fluoroorgano boron compounds that can beused as co-catalysts in the present invention can include, but are notlimited to, tris(pentafluorophenyl)boron,tris[3,5-bis(trifluoromethyl)-phenyl]boron, and the like, or mixturesthereof. Although not intending to be bound by the following theory,these examples of fluoroorgano borate and fluoroorgano boron compounds,and related compounds, can form “weakly-coordinating” anions whencombined with a transition metal complex (see e.g., U.S. Pat. No.5,919,983, the disclosure of which is incorporated herein by referencein its entirety). Applicants also contemplate the use of diboron, orbis-boron, compounds or other bifunctional compounds containing two ormore boron atoms in the chemical structure, such as disclosed in J. Am.Chem. Soc., 2005, 127, pp. 14756-14768, the content of which isincorporated herein by reference in its entirety.

Generally, any amount of organoboron compound can be used. According toone aspect of this invention, the molar ratio of the total moles oforganoboron or organoborate compound (or compounds) to the total molesof transition metal complex (or complexes) in the catalyst compositioncan be in a range from about 0.1:1 to about 15:1. Typically, the amountof the fluoroorgano boron or fluoroorgano borate compound used can befrom about 0.5 moles to about 10 moles of boron/borate compound per moleof transition metal complex(es). According to another aspect of thisinvention, the amount of fluoroorgano boron or fluoroorgano boratecompound can be from about 0.8 moles to about 5 moles of boron/boratecompound per mole of transition metal complex(es).

Ionizing Ionic Compounds

In another embodiment, catalyst compositions disclosed herein cancomprise an ionizing ionic compound. An ionizing ionic compound is anionic compound that can function as a co-catalyst to enhance theactivity of the catalyst composition. While not intending to be bound bytheory, it is believed that the ionizing ionic compound can be capableof reacting with a transition metal complex and converting thetransition metal complex into one or more cationic transition metalcomplexes, or incipient cationic transition metal complexes. Again,while not intending to be bound by theory, it is believed that theionizing ionic compound can function as an ionizing compound bycompletely or partially extracting an anionic ligand, such as X¹ or X²,from the transition metal complex. However, the ionizing ionic compoundcan be a co-catalyst regardless of whether it is ionizes the transitionmetal complex, abstracts a X¹ or X² ligand in a fashion as to form anion pair, weakens the metal-X¹ or metal-X² bond in the transition metalcomplex, simply coordinates to a X¹ or X² ligand, or activates thetransition metal complex by some other mechanism.

Further, it is not necessary that the ionizing ionic compound activatethe transition metal complex only. The activation function of theionizing ionic compound can be evident in the enhanced activity ofcatalyst composition as a whole, as compared to a catalyst compositionthat does not contain an ionizing ionic compound.

Examples of ionizing ionic compounds can include, but are not limitedto, the following compounds: tri(n-butyl)ammoniumtetrakis(p-tolyl)borate, tri(n-butyl) ammonium tetrakis(m-tolyl)borate,tri(n-butyl)ammonium tetrakis(2,4-dimethylphenyl)borate,tri(n-butyl)ammonium tetrakis(3,5-dimethylphenyl)borate,tri(n-butyl)ammonium tetrakis[3,5-bis(trifluoromethyl)phenyl]borate,tri(n-butyl)ammonium tetrakis(pentafluorophenyl)borate.N,N-dimethylanilinium tetrakis(p-tolyl)borate, N,N-dimethylaniliniumtetrakis(m-tolyl)borate, N,N-di methylaniliniumtetrakis(2,4-dimethylphenyl)borate, N,N-dimethylaniliniumtetrakis(3,5-dimethylphenyl)borate, N,N-dimethylaniliniumtetrakis[3,5-bis(trifluoro-methyl)phenyl]borate, N,N-dimethylaniliniumtetrakis(pentafluorophenyl)borate, triphenylcarbeniumtetrakis(p-tolyl)borate, triphenylcarbenium tetrakis(m-tolyl)borate,triphenylcarbenium tetrakis(2,4-dimethylphenyl)borate,triphenylcarbenium tetrakis(3,5-dimethylphenyl)borate,triphenylcarbenium tetrakis[3,5-bis(trifluoromethyl)phenyl]borate,triphenylcarbenium tetrakis(pentafluorophenyl)borate, tropyliumtetrakis(p-tolyl)borate, tropylium tetrakis(m-tolyl)borate, tropyliumtetrakis(2,4-dimethylphenyl)borate, tropyliumtetrakis(3,5-dimethylphenyl)borate, tropyliumtetrakis[3,5-bis(trifluoromethyl)phenyl]borate, tropyliumtetrakis(pentafluorophenyl)borate, lithiumtetrakis(pentafluorophenyl)borate, lithium tetraphenylborate, lithiumtetrakis(p-tolyl)borate, lithium tetrakis(m-tolyl)borate, lithiumtetrakis(2,4-dimethylphenyl)borate, lithiumtetrakis(3,5-dimethylphenyl)borate, lithium tetrafluoroborate, sodiumtetrakis(pentafluorophenyl)borate, sodium tetraphenylborate, sodiumtetrakis(p-tolyl)borate, sodium tetrakis(m-tolyl)borate, sodiumtetrakis(2,4-dimethylphenyl)borate, sodiumtetrakis(3,5-dimethylphenyl)borate, sodium tetrafluoroborate, potassiumtetrakis(pentafluorophenyl)borate, potassium tetraphenylborate,potassium tetrakis(p-tolyl)borate, potassium tetrakis(m-tolyl)borate,potassium tetrakis(2,4-dimethyl-phenyl)borate, potassiumtetrakis(3,5-dimethylphenyl)borate, potassium tetrafluoroborate, lithiumtetrakis(pentafluorophenyl)aluminate, lithium tetraphenylaluminate,lithium tetrakis(p-tolyl)aluminate, lithium tetrakis(m-tolyl)aluminate,lithium tetrakis(2,4-dimethylphenyl)aluminate, lithiumtetrakis(3,5-dimethylphenyl)aluminate, lithium tetrafluoroaluminate,sodium tetrakis(pentafluorophenyl)aluminate, sodiumtetraphenylaluminate, sodium tetrakis(p-tolyl)aluminate, sodiumtetrakis(m-tolyl)aluminate, sodiumtetrakis(2,4-dimethylphenyl)aluminate, sodiumtetrakis(3,5-dimethylphenyl)aluminate, sodium tetrafluoroaluminate,potassium tetrakis(pentafluorophenyl)aluminate, potassiumtetraphenylaluminate, potassium tetrakis(p-tolyl)aluminate, potassiumtetrakis(m-tolyl)-aluminate, potassiumtetrakis(2,4-dimethylphenyl)aluminate, potassiumtetrakis(3,5-dimethylphenyl)aluminate, potassium tetrafluoroaluminate,and the like, or combinations thereof. Ionizing ionic compounds usefulin this invention are not limited to these; other examples of ionizingionic compounds are disclosed in U.S. Pat. Nos. 5,576,259 and 5,807,938,the disclosures of which are incorporated herein by reference in theirentirety.

Organozinc, Organomagnesium, & Organolithium Compounds

Other embodiments are directed to catalyst compositions which caninclude an organozinc compound, an organomagnesium compound, anorganolithium compound, or a combination thereof. In some aspects, thesecompounds have the following general formulas:Zn(X¹⁰)(X¹¹);Mg(X¹²)(X¹³); andLi(X¹⁴).In these formulas, X¹⁰, X¹², and X¹⁴ independently can be a C₁ to C₁₈hydrocarbyl group, and X¹¹ and X¹³ independently can be H, a halide, ora C₁ to C₁₈ hydrocarbyl or C₁ to C₁₈ hydrocarboxy group. It iscontemplated X¹⁰ and X¹¹ (or X¹² and X¹³) can be the same, or that X¹⁰and X¹¹ (or X¹² and X¹³) can be different.

In one aspect, X¹⁰, X¹¹, X¹², X¹³, and X¹⁴ independently can be any C₁to C₁₈ hydrocarbyl group, C₁ to C₁₂ hydrocarbyl group, C₁ to C₈hydrocarbyl group, or C₁ to C₅ hydrocarbyl group disclosed herein. Inanother aspect, X¹⁰, X¹¹, X¹², X¹³, and X¹⁴ independently can be any C₁to C₁₈ alkyl group, C₂ to C₁₈ alkenyl group, C₆ to C₁₈ aryl group, or C₇to C₁₈ aralkyl group disclosed herein; alternatively, any C₁ to C₁₂alkyl group, C₂ to C₁₂ alkenyl group, C₆ to C₁₂ aryl group, or C₇ to C₁₂aralkyl group disclosed herein; or alternatively, any C₁ to C₅ alkylgroup, C₂ to C₅ alkenyl group, C₆ to C₈ aryl group, or C₇ to C₈ aralkylgroup disclosed herein. Thus, X¹⁰, X¹¹, X¹², X¹³, and X¹⁴ independentlycan be a methyl group, an ethyl group, a propyl group, a butyl group, apentyl group, a hexyl group, a heptyl group, an octyl group, a nonylgroup, a decyl group, a undecyl group, a dodecyl group, a tridecylgroup, a tetradecyl group, a pentadecyl group, a hexadecyl group, aheptadecyl group, an octadecyl group, an ethenyl group, a propenylgroup, a butenyl group, a pentenyl group, a hexenyl group, a heptenylgroup, an octenyl group, a nonenyl group, a decenyl group, a undecenylgroup, a dodecenyl group, a tridecenyl group, a tetradecenyl group, apentadecenyl group, a hexadecenyl group, a heptadecenyl group, anoctadecenyl group, a phenyl group, a naphthyl group, a benzyl group, ora tolyl group, and the like. In yet another aspect, X¹⁰, X¹¹, X¹², X¹³,and X¹⁴ independently can be methyl, ethyl, propyl, butyl, or pentyl(e.g., neopentyl), or both X¹⁰ and X¹¹ (or both X¹² and X¹³) can bemethyl, or ethyl, or propyl, or butyl, or pentyl (e.g., neopentyl).

X¹¹ and X¹³ independently can be H, a halide, or a C₁ to C₁₈ hydrocarbylor C₁ to C₁₈ hydrocarboxy group (e.g., any C₁ to C₁₈, C₁ to C₁₂, C₁ toC₁₀, or C₁ to C₈ hydrocarboxy group disclosed herein). In some aspects,X¹¹ and X¹³ independently can be H, a halide (e.g., Cl), or a C₁ to C₁₈hydrocarbyl or C₁ to C₁₈ hydrocarboxy group; alternatively, H, a halide,or a C₁ to C₈ hydrocarbyl or C₁ to C₈ hydrocarboxy group; oralternatively, H, Br, Cl, F, I, methyl, ethyl, propyl, butyl, pentyl(e.g., neopentyl), hexyl, heptyl, octyl, nonyl, decyl, ethenyl,propenyl, butenyl, pentenyl, hexenyl, heptenyl, octenyl, nonenyl,decenyl, phenyl, benzyl, tolyl, methoxy, ethoxy, propoxy, butoxy,pentoxy, phenoxy, toloxy, xyloxy, or benzoxy.

In other aspects, the organozinc and/or the organomagnesium compound canhave one or two hydrocarbylsilyl moieties. Each hydrocarbyl of thehydrocarbylsilyl group can be any hydrocarbyl group disclosed herein(e.g., a C₁ to C₁₈ alkyl group, a C₂ to C₁₈ alkenyl group, a C₆ to C₁₈aryl group, a C₇ to C₁₈ aralkyl group, etc.). Illustrative andnon-limiting examples of hydrocarbylsilyl groups can include, but arenot limited to, trimethylsilyl, triethylsilyl, tripropylsilyl (e.g.,triisopropylsilyl), tributylsilyl, tripentylsilyl, triphenylsilyl,allyklimethylsilyl, trinethylsilylmethyl, and the like.

Exemplary organozinc compounds which can be used as co-catalysts caninclude, but are not limited to, dimethylzinc, diethylzinc,dipropylzinc, dibutylzinc, dineopentylzinc, di(trimethylsilyl)zinc,di(triethylsilyl)zinc, di(triisoproplysilyl)zinc,di(triphenylsilyl)zinc, di(allyldimethylsilyl)zinc,di(trimethylsilylmethyl)zinc, and the like, or combinations thereof.

Similarly, exemplary organomagnesium compounds can include, but are notlimited to, dimethylmagnesium, diethylmagnesium, dipropylmagnesium,dibutylmagnesium, dineopentylmagnesium,di(trimethylsilylmethyl)magnesium, methylmagnesium chloride,ethylmagnesium chloride, propylinagnesium chloride, butylmagnesiumchloride, neopentylmagnesium chloride, trimethylsilylmethylmagnesiumchloride, methylmagnesium bromide, ethylmagnesium bromide,propylmagnesium bromide, butylmagnesium bromide, neopentylmagnesiumbromide, trimethylsilylmethylmagnesium bromide, methylmagnesium iodide,ethylmagnesium iodide, propylmagnesium iodide, butyl magnesium iodide,neopentylmagnesium iodide, trimethylsilylmethylmagnesium iodide,methylmagnesium ethoxide, ethylmagnesium ethoxide, propylmagnesiumethoxide, butylmagnesium ethoxide, neopentylmagnesium ethoxide,trimethylsilylmethylmagnesium ethoxide, methylmagnesium propoxide,ethylmagnesium propoxide, propylmagnesium propoxide, butylmagnesiumpropoxide, neopentylmagnesium propoxide, trimethylsilylmethylmagnesiumpropoxide, methylmagnesium phenoxide, ethylmagnesium phenoxide,propylmagnesium phenoxide, butylmagnesium phenoxide, neopentylmagnesiumphenoxide, trimethylsilylmethylmagnesium phenoxide, and the like, or anycombinations thereof.

Likewise, exemplary organolithium compounds can include, but are notlimited to, methyllithium, ethyllithium, propyllithium, butyllithium(e.g., t-butyllithium), neopentyllithium, trimethylsilylmethyllithium,phenyllithium, tolyllithiutn, xylyllithium, benzyllithium,(dimethylphenyl)methyllithium, allyllithium, and the like, orcombinations thereof.

Catalyst Compositions

Consistent with embodiments disclosed herein are various catalystsystems and compositions. A composition in accordance with an embodimentof the invention can comprise an amine bis(phenolate) transition metalcomplex (e.g., an N,N-bis[2-hydroxidebenzyl]amine transition metalcompound). In another embodiment, a catalyst composition can comprise atransition metal complex, an activator-support, and an optionalco-catalyst. In one aspect, the present invention can encompass catalystcompositions comprising a transition metal complex, a chemically-treatedsolid oxide, and an organoaluminum compound, while in another aspect,the present invention can encompass catalyst compositions comprising atransition metal complex, a chemically-treated solid oxide, and aco-catalyst comprising an aluminoxane compound, an organoboron ororganoborate compound, an ionizing ionic compound, an organoaluminumcompound, an organozinc compound, an organomagnesium compound, or anorganolithium compound, or any combination thereof. These catalystcompositions can be utilized to produce alpha olefin polymer (oroligomer) products for a variety of end-use applications.

Transition metal complexes or compounds having formulas (Ia), (Ib),(IIa), (IIb), (IIIa), and/or (IIIb) were discussed above. In aspects ofthe present invention, it is contemplated that the catalyst compositioncan contain more than one transition metal compound having formula (Ia),(Ib), (IIa), (IIb), (IIIa), and/or (IIIb). Further, additional catalyticcompounds (e.g., metallocene compounds)—other than those having formulas(Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb)—can be employed in thecatalyst composition and/or the polymerization process, provided thatthe additional catalytic compound(s) does not detract from theadvantages disclosed herein. Additionally, more than oneactivator-support and/or more than one co-catalyst also can be utilizedin the catalyst composition.

Generally, catalyst compositions of the present invention can comprise atransition metal complex having formula (Ia), (Ib), (Ia), (IIb), (IIIa),and/or (IIIb) and an activator-support. In aspects of the invention, theactivator-support can comprise a solid oxide treated with anelectron-withdrawing anion. Activator-supports useful in the presentinvention were disclosed above. Optionally, such catalyst compositionscan further comprise one or more than one organoaluminum compound orcompounds (suitable organoaluminum compounds also were discussed above).Thus, a catalyst composition of this invention can comprise a transitionmetal complex having formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or(IIIb), an activator-support, and an organoaluminum compound. Forinstance, the activator-support can comprise (or consist essentially of,or consist of) fluorided alumina, chlorided alumina, bromided alumina,sulfated alumina, fluorided silica-alumina, chlorided silica-alumina,bromided silica-alumina, sulfated silica-alumina, fluoridedsilica-zirconia, chlorided silica-zirconia, bromided silica-zirconia,sulfated silica-zirconia, fluorided silica-titania, fluoridedsilica-coated alumina, sulfated silica-coated alumina, phosphatedsilica-coated alumina, and the like, or combinations thereof.Additionally, the organoaluminum compound can comprise (or consistessentially of, or consist of) trimethylaluminum, triethylaluminum,tri-n-propylaluminun, tri-n-butylaluminum, triisobutylaluminum,tri-n-hexylaluminum, tri-n-octylaluminum, diisobutylaluminum hydride,diethylaluminum ethoxide, diethylaluminum chloride, and the like, orcombinations thereof. Accordingly, a catalyst composition consistentwith aspects of the invention can comprise (or consist essentially of,or consist of) a transition metal compound having formula (Ia), (Ib),(Ia), (IIb), (IIIa), and/or (IIIb), sulfated alumina (or fluoridedsilica-alumina, or fluorided silica-coated alumina), andtriethylaluminum (or triisobutylaluminum).

In another aspect of the present invention, a catalyst composition isprovided which comprises a transition metal complex having formula (Ia),(Ib), (IIa), (IIb), (IIIa), and/or (IIIb), an activator-support, and anorganoaluminum compound, wherein this catalyst composition issubstantially free of aluminoxanes, organoboron or organoboratecompounds, ionizing ionic compounds, and/or other similar co-catalysts;alternatively, substantially free of aluminoxanes; alternatively,substantially free or organoboron or organoborate compounds; oralternatively, substantially free of ionizing ionic compounds. In theseaspects, the catalyst composition has catalyst activity in the absenceof these additional materials. For example, a catalyst composition ofthe present invention can consist essentially of a transition metalcomplex having formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb),an activator-support, and an organoaluminum compound, wherein no othermaterials are present in the catalyst composition which wouldincrease/decrease the activity of the catalyst composition by more thanabout 10% from the catalyst activity of the catalyst composition in theabsence of said materials.

However, in other aspects of this invention, these co-catalysts can beemployed. For example, a catalyst composition comprising a transitionmetal complex having formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or(IIIb) and an activator-support can further comprise an optionalco-catalyst. Suitable co-catalysts in this aspect can include, but arenot limited to, aluminoxane compounds, organoboron or organoboratecompounds, ionizing ionic compounds, organoaluminum compounds,organozinc compounds, organomagnesium compounds, organolithiumcompounds, and the like, or any combination thereof.

In a different aspect, a catalyst composition is provided which containsa co-catalyst other than an organoaluminum compound. Such a catalystcomposition can comprise a transition metal complex having formula (Ia),(Ib), (IIa), (IIb), (IIIa), and/or (IIIb), an activator-support, and aco-catalyst, wherein the co-catalyst comprises an aluminoxane compound,an organoboron or organoborate compound, an ionizing ionic compound, anorganozinc compound, an organomagnesium compound, an organolithiumcompound, and the like, or any combination thereof.

This invention further encompasses methods of making these catalystcompositions, such as, for example, contacting the respective catalystcomponents in any order or sequence.

The transition metal complex having formula (Ia), (Ib), (IIa), (IIb),(IIIa), and/or (IIIb) can be precontacted with an olefinic monomer ifdesired, not necessarily the olefin monomer to be polymerized, and anorganoaluminum compound for a first period of time prior to contactingthis precontacted mixture with an activator-support. The first period oftime for contact, the precontact time, between the transition metalcomplex, the olefinic monomer, and the organoaluminum compound typicallyranges from a time period of about 1 minute to about 24 hours, forexample, from about 3 minutes to about 1 hour. Precontact times fromabout 10 minutes to about 30 minutes also can be employed.Alternatively, the precontacting process can be carried out in multiplesteps, rather than a single step, in which multiple mixtures can beprepared, each comprising a different set of catalyst components. Forexample, at least two catalyst components can be contacted forming afirst mixture, followed by contacting the first mixture with at leastone other catalyst component forming a second mixture, and so forth.

Multiple precontacting steps can be carried out in a single vessel or inmultiple vessels. Further, multiple precontacting steps can be carriedout in series (sequentially), in parallel, or a combination thereof. Forexample, a first mixture of two catalyst components can be formed in afirst vessel, a second mixture comprising the first mixture plus oneadditional catalyst component can be formed in the first vessel or in asecond vessel, which is typically placed downstream of the first vessel.

In another aspect, one or more of the catalyst components can be splitand used in different precontacting treatments. For example, part of acatalyst component can be fed into a first precontacting vessel forprecontacting with at least one other catalyst component, while theremainder of that same catalyst component can be fed into a secondprecontacting vessel for precontacting with at least one other catalystcomponent, or can be fed directly into the reactor, or a combinationthereof. The precontacting can be carried out in any suitable equipment,such as tanks, stirred mix tanks, various static mixing devices, aflask, a vessel of any type, or combinations of these apparatus.

In another aspect of this invention, the various catalyst components(for example, a transition metal complex having formula (Ia), (Ib),(IIa), (IIb), (IIIa), and/or (IIIb), an activator-support, anorganoaluminum co-catalyst, and optionally an unsaturated hydrocarbon)can be contacted in the polymerization reactor simultaneously while thepolymerization reaction is proceeding. Alternatively, any two or more ofthese catalyst components can be precontacted in a vessel prior toentering the reaction zone. This precontacting step can be continuous,in which the precontacted product can be fed continuously to thereactor, or it can be a stepwise or batchwise process in which a batchof precontacted product can be added to make a catalyst composition.This precontacting step can be carried out over a time period that canrange from a few seconds to as much as several days, or longer. In thisaspect, the continuous precontacting step generally can last from about1 second to about 1 hour. In another aspect, the continuousprecontacting step can last from about 10 seconds to about 45 minutes,or from about 1 minute to about 30 minutes.

Once the precontacted mixture of the transition metal compound havingformula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), the olefinmonomer, and the organoaluminum co-catalyst is contacted with theactivator-support, this composition (with the addition of theactivator-support) can be termed the “postcontacted mixture.” Thepostcontacted mixture optionally can remain in contact for a secondperiod of time, the postcontact time, prior to initiating thepolymerization process. Postcontact times between the precontactedmixture and the activator-support generally range from about 1 minute toabout 24 hours. In a further aspect, the postcontact time can be in arange from about 3 minutes to about 1 hour. The precontacting step, thepostcontacting step, or both, can increase the productivity of thepolymer as compared to the same catalyst composition that is preparedwithout precontacting or postcontacting. However, neither aprecontacting step nor a postcontacting step is required.

The postcontacted mixture can be heated at a temperature and for a timeperiod sufficient to allow adsorption, impregnation, or interaction ofprecontacted mixture and the activator-support, such that a portion ofthe components of the precontacted mixture can be immobilized, adsorbed,or deposited thereon. Where heating is employed, the postcontactedmixture generally can be heated to a temperature of from between about−15° C. to about 70° C., or from about 0° C. to about 40° C.

When a precontacting step is used, the molar ratio of the total moles ofolefin monomer to total moles of transition metal compound(s) in theprecontacted mixture typically can be in a range from about 1:10 toabout 100,000:1. Total moles of each component are used in this ratio toaccount for aspects of this invention where more than one olefin monomerand/or more than one transition metal complex is employed in aprecontacting step. Further, this molar ratio can be in a range fromabout 10:1 to about 1,000:1 in another aspect of the invention.

Generally, the weight ratio of organoaluminum compound toactivator-support can be in a range from about 10:1 to about 1:1000. Ifmore than one organoaluminum compound and/or more than oneactivator-support is employed, this ratio is based on the total weightof each respective component. In another aspect, the weight ratio of theorganoaluminum compound to the activator-support can be in a range fromabout 3:1 to about 1:100, or from about 1:1 to about 1:50.

In some aspects of this invention, the weight ratio of transition metalcompound(s) to activator-support can be in a range from about 1:1 toabout 1:1,000,000. If more than one activator-support is employed, thisratio is based on the total weight of the activator-support. In anotheraspect, this weight ratio can be in a range from about 1:5 to about1:100,000, or from about 1:10 to about 1:10,000. Yet, in another aspect,the weight ratio of the transition metal compound(s) to theactivator-support can be in a range from about 1:20 to about 1:1000.

As discussed above, any combination of the transition metal compoundhaving formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), theactivator-support, the organoaluminum compound, and the olefin monomer,can be precontacted in some aspects of this invention. When anyprecontacting occurs with an olefinic monomer, it is not necessary thatthe olefin monomer used in the precontacting step be the same as theolefin to be polymerized. Further, when a precontacting step among anycombination of the catalyst components is employed for a first period oftime, this precontacted mixture can be used in a subsequentpostcontacting step between any other combination of catalyst componentsfor a second period of time. For example, the transition metal compound,the organoaluminum compound, and 1-hexene can be used in a precontactingstep for a first period of time, and this precontacted mixture then canbe contacted with the activator-support to form a postcontacted mixturethat can be contacted for a second period of time prior to initiatingthe polymerization reaction. For example, the first period of time forcontact, the precontact time, between any combination of the transitionmetal compound, the olefinic monomer, the activator-support, and theorganoaluminum compound can be from about 1 minute to about 24 hours,from about 3 minutes to about 1 hour, or from about 10 minutes to about30 minutes. The postcontacted mixture optionally can be allowed toremain in contact for a second period of time, the postcontact time,prior to initiating the polymerization process. According to one aspectof this invention, postcontact times between the precontacted mixtureand any remaining catalyst components can be from about 1 minute toabout 24 hours, or from about 5 minutes to about 1 hour.

Alpha Olefin Monomers, Alpha Olefin Products, and Articles

A wide range of alpha olefin monomers can be polymerized (oroligomerized) according to the methods provided herein, and using thecatalyst compositions disclosed herein. In some embodiments, forexample, alpha olefin polymerization (or oligomerization) products canbe produced from an alpha olefin monomer comprising, or consistingessentially of, a C₃ to C₇₀ alpha olefin; alternatively, a C₃ to C₆₀alpha olefin; alternatively, a C₄ to C₆₀ alpha olefin; alternatively, aC₅ to C₁₈ alpha olefin; alternatively, a C₆ to C₁₄ alpha olefin; oralternatively, a C₈ to C₁₂ alpha olefin. In other embodiments, alphaolefin oligomer products can be produced from an alpha olefin monomercomprising, or consisting essentially of, a C₆ alpha olefin, a C₈ alphaolefin, a C₁₀ alpha olefin, a C₁₂ alpha olefin, a C₁₄ alpha olefin, aC₁₆ alpha olefin, or any combination thereof; alternatively, a Ca alphaolefin, a C₁₀ alpha olefin, a C₂ alpha olefin, or any combinationthereof; alternatively, a C₆ alpha olefin; alternatively, a C₈ alphaolefin; alternatively, a C₁₀ alpha olefin; alternatively, a C₁₂ alphaolefin; alternatively, a C₁₄ alpha olefin; alternatively, a C₁₆ alphaolefin; or alternatively, a C₁₈ alpha olefin. In an aspect, the alphaolefin product can be produced from an alpha olefin monomer comprising,or consisting essentially of, a C₃ to C₇₀ linear alpha olefin;alternatively, a C₄ to C₆₀ linear alpha olefin; alternatively, a C₄ toC₂₀ linear alpha olefin; alternatively, a C₅ to C₁₂ linear alpha olefin;alternatively, a C₆ to C₁₄ linear alpha olefin; or alternatively, a C₈to C₁₂ linear alpha olefin. In another aspect, the alpha olefin productcan be produced from an alpha olefin monomer comprising, or consistingessentially of, a C₃ to C₇₀ normal alpha olefin; alternatively, a C₄ toCo normal alpha olefin; alternatively, a C₄ to C₂₀ normal alpha olefin;alternatively, a C₅ to C₁₈ normal alpha olefin; alternatively, a C₆ toC₁₄ normal alpha olefin; or alternatively, a C₈ to C₁₂ normal alphaolefin. In yet another aspect, the alpha olefin product can be producedfrom an alpha olefin monomer comprising, or consisting essentially of, aC₆ normal alpha olefin, a C₈ normal alpha olefin, a C₁₀ normal alphaolefin, a C₁₂ normal alpha olefin, a C₁₄ normal alpha olefin, a C₁₆normal alpha olefin, or any combination thereof; alternatively, a C₈normal alpha olefin, a C₁₀ normal alpha olefin, a C₁₂ normal alphaolefin, or any combination thereof; alternatively, a C₆ normal alphaolefin; alternatively, a C₈ normal alpha olefin; alternatively, a C₁₀normal alpha olefin; alternatively, a C₁₂ normal alpha olefin;alternatively, a C₁₄ normal alpha olefin; alternatively, a C₁₆ normalalpha olefin; or alternatively, a C₁₈ normal alpha olefin.

In another aspect, the alpha olefin polymer (or oligomer) product can beproduced from an alpha olefin monomer comprising, or consistingessentially of, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene,1-nonene, 1-decene, 1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene,1-pentadecene, 1-hexadecene, 1-heptadecene, 1-octadecene, or anycombination thereof; alternatively, 1-hexene, 1-heptene, 1-octene,1-nonene, 1-decene, 1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene,1-pentadecene, 1-hexadecene, or any combination thereof; oralternatively, 1-octene, 1-nonene, 1-decene, 1-undecene, 1-dodecene, orany combination thereof. In yet another aspect, the alpha olefin productcan be produced from an alpha olefin monomer comprising, or consistingessentially of, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene,1-hexadecene, or any combination thereof, alternatively, 1-hexene,1-octene, 1-decene, 1-tetradecene, or any combination thereof. In stillanother aspect, the alpha olefin product can be produced from an alphaolefin monomer comprising, or consisting essentially of, 1-butene;alternatively, 1-pentene; alternatively, 1-hexene; alternatively,1-heptene; alternatively, 1-octene; alternatively, 1-nonene;alternatively, 1-decene; alternatively, 1-undecene; alternatively,1-dodecene; alternatively, 1-tridecene; alternatively, 1-tetradecene;alternatively, 1-pentadecene; alternatively, 1-hexadecene;alternatively, 1-heptadecene; or alternatively, 1-octadecene.

In an aspect, the alpha olefin product can be produced from an alphaolefin monomer comprising, or consisting essentially of, an alpha olefinhaving the formula CH₂═CH(CH₂)_(n)CH₃, wherein n can be an integer from1 to 17; alternatively, having the formula CH₂═CH(CH₂)_(n)CH₃, wherein ncan be an integer from 2 to 15; alternatively, having the formulaCH₂═CH(CH₂)_(n)CH₃, wherein n can be an integer from 3 to 13; oralternatively, having the formula CH₂═CH(CH₂)_(n)CH₃, wherein n can bean integer from 5 to 9. In another aspect, the alpha olefin product canbe produced from an alpha olefin monomer comprising, or consistingessentially of, an alpha olefin having the formula CH₂═CH(CH₂)_(n)CH₃,wherein n can be 3; alternatively, an alpha olefin having the formulaCH₂═CH(CH₂)_(n)CH₃, wherein n can be 5; alternatively, an alpha olefinhaving the formula CH₂═CH(CH₂)_(n)CH₃, wherein n can be 7;alternatively, an alpha olefin having the formula CH₂═CH(CH₂)_(n)CH₃,wherein n can be 9; alternatively, an alpha olefin having the formulaCH₂═CH(CH₂)_(n)CH₃, wherein n can be 11; alternatively, an alpha olefinhaving the formula CH₂═CH(CH)_(n)CH₃, wherein n can be 13; oralternatively, an alpha olefin having the formula CH₂═CH(CH)_(n)CH₃,wherein n can be 15.

In an aspect, the alpha olefin product which can be produced accordingto the methods described herein can be produced using an olefin monomercomprising, or consisting essentially of, a blend or mixture of alphaolefins; or alternatively, a blend or mixture of normal alpha olefins.Generally, the olefin monomer can be a blend or mixture of any alphaolefin described herein, or alternatively, any normal alpha olefin,described herein. In one aspect, the blend of alpha olefins can compriseat least 50 weight percent, at least 60 weight percent, at least 70weight percent, at least 75 weight percent, at least 80 weight percent,at least 85 weight percent, at least 90 weight percent, at least 92.5weight percent, or at least 95 weight percent of any carbon number rangeof alpha olefins described herein; alternatively, of any combination ofsingle carbon numbered alpha olefins described herein; or alternatively,of any single carbon numbered alpha olefin described herein. In anotheraspect, the blend or mixture of normal alpha olefins can comprise atleast 50 weight percent, at least 60 weight percent, at least 70 weightpercent, at least 75 weight percent, at least 80 weight percent, atleast 85 weight percent, at least 90 weight percent, at least 92.5weight percent, or at least 95 weight percent of any carbon numberedrange of normal alpha olefins described herein; alternatively, anycombination of single carbon numbered normal alpha olefins describedherein; or alternatively, any single numbered normal alpha olefindescribed herein.

In a non-limiting example, the olefin monomer can comprise a blend ofalpha olefins comprising at least 80 weight percent of C₆ to C₁₆ alphaolefins; alternatively, at least 60 weight percent of a C₆ alpha olefinand C₁₄ alpha olefin; alternatively, at least 90 weight percent of a C₈to C₁₂ normal alpha olefin; alternatively, at least 85 weight percent of1-hexene, 1-decene, and 1-tetradecene; alternatively, at least 75 weightpercent 1-octene; or alternatively, at least 75 weight percent of anormal alpha olefin consisting essentially of 1-octene. In anothernon-limiting example, the single carbon numbered alpha olefin which canbe utilized in an alpha olefin blend can consist essentially of a C₆alpha olefin; alternatively, a C₈ alpha olefin; alternatively, a C₁₀alpha olefin; alternatively, a C₁₂ alpha olefin; alternatively, a C₁₄alpha olefin; or alternatively, a C₁₆ alpha olefin. In yet anothernon-limiting example, the single carbon numbered normal alpha olefinwhich can be utilized in an alpha olefin blend or normal alpha olefinblend can consist essentially of a C₆ normal alpha olefin;alternatively, a C₈ normal alpha olefin; alternatively, a C₁₀ normalalpha olefin; alternatively, a C₁₂ normal alpha olefin; alternatively, aC₁₄ normal alpha olefin; or alternatively, a C₁₆ normal alpha olefin.Other potential blends of alpha olefin and/or normal alpha olefinmonomer which can be utilized are readily apparent from the presentdisclosure.

As described, the alpha olefin product can be produced bypolymerizing/oligomerizing an alpha olefin monomer. These alpha olefinproducts comprise units derived from the alpha olefin monomer(s). Onehaving ordinary skill in the art will recognize that a catalyst systemutilized to form the alpha olefin product can, in some aspects,isomerize the alpha olefin monomer to a non-alpha olefin (e.g., aninternal olefin). Alternatively or additionally, the alpha olefinfeedstock can contain quantities of non-alpha olefins. Depending uponthe catalyst system utilized, the non-alpha olefins can be incorporatedinto the alpha olefin oligomer or polymer (and such that the resultingproduct can contain alpha olefin monomer units in combination withinternal olefin monomer units). In some instances, the catalyst systemcan limit the extent of alpha olefin isomerization and/or limit thequantity of non-alpha olefins incorporated into the alpha olefinoligomer. Consequently, one feature of the alpha olefinpolymerization/oligomerization product can be the percentage of alphaolefin units in the alpha olefin product. Thus, in any disclosed aspector embodiment, the alpha olefin product described herein can comprise atleast 70 percent alpha olefin monomer units; alternatively, at least 75percent alpha olefin monomer units; alternatively, at least 80 percentalpha olefin monomer units; alternatively, at least 85 percent alphaolefin monomer units; alternatively, at least 90 percent alpha olefinmonomer units; alternatively, at least 95 percent alpha olefin monomerunits; alternatively, at least 98 percent alpha olefin monomer units; oralternatively, at least 99 percent alpha olefin monomer units. In afurther aspect, the alpha olefin product can consist essentially ofalpha olefin monomer units, and the alpha olefin can be any alpha olefindescribed herein.

In an aspect, the collection of alpha olefin monomer and alpha olefinproduct in the reactor effluent or the alpha olefin product according tothis disclosure can comprise less than 20 weight % alpha olefin monomer,alternatively, less than 17.5 weight % alpha olefin monomer;alternatively, less than 15 weight % alpha olefin monomer;alternatively, less than 12.5 weight % alpha olefin monomer;alternatively, less than 10 weight % alpha olefin monomer;alternatively, less than 9 weight % alpha olefin monomer, alternatively,less than 8 weight % alpha olefin monomer; alternatively, less than 7weight % alpha olefin monomer; alternatively, less than 6 weight % alphaolefin monomer; alternatively, less than 5 weight % alpha olefinmonomer, alternatively, less than 4 weight % alpha olefin monomer;alternatively, less than 3 weight % alpha olefin monomer, alternatively,less than 2 weight % alpha olefin monomer; alternatively, less than 1weight % alpha olefin monomer, alternatively, less than 0.8 weight %alpha olefin monomer, alternatively, less than 0.6 weight % alpha olefinmonomer, alternatively, less than 0.5 weight % alpha olefin monomer;alternatively, less than 0.4 weight % alpha olefin monomer,alternatively, less than 0.3 weight % alpha olefin monomer;alternatively, less than 0.2 weight % alpha olefin monomer; oralternatively, less than 0.1 weight % alpha olefin monomer. In anotheraspect, the alpha olefin monomer content can be referred to as residualalpha olefin monomer (e.g., a separated reactor effluent) and can be anyalpha olefin monomer content described herein. In another aspect, thecollection of alpha olefin monomer and alpha olefin product in thereactor effluent or the alpha olefin product according to thisdisclosure can comprise less than 20 weight % dimers; alternatively,less than 19 weight % dimers; alternatively, less than 18 weight %dimers; alternatively, less than 17 weight % dimers; alternatively, lessthan 16 weight % dimers; alternatively, less than 15 weight % dimers;alternatively, less than 14 weight % dimers; alternatively, less than 13weight % dimers; alternatively, less than 12 weight % dimers;alternatively, less than 11 weight % dimers; alternatively, less than 10weight % dimers; alternatively, less than 9 weight % dimers;alternatively, less than 8 weight % dimers; alternatively, less than 7weight % dimers; alternatively, less than 6 weight % dimers;alternatively, less than 5 weight % dimers; alternatively, less than 4weight % dimers; less than 3 weight % dimers; less than 2.5 weight %dimers; alternatively, less than 2 weight % dimers; alternatively, lessthan 1.75 weight % dimers; alternatively, less than 1.5 weight % dimers;alternatively, less than 1.25 weight % dimers; alternatively, less than1 weight % dimers; alternatively, less than 0.9 weight % dimers;alternatively, less than 0.8 weight % dimers; alternatively, less than0.7 weight % dimers; alternatively, less than 0.6 weight % dimers;alternatively, less than 0.5 weight % dimers; alternatively, less than0.4 weight % dimers; or alternatively, less than 0.3 weight % dimers. Inanother aspect, the collection of alpha olefin monomer and alpha olefinproduct in the reactor effluent or the alpha olefin product according tothis disclosure can comprise less than 20 weight % trimers;alternatively, less than 17.5 weight % trimers; alternatively, less than15 weight % trimers; alternatively, less than 12.5 weight % trimers;alternatively, less than 10 weight % trimers; less than 7.5 weight %trimers; alternatively, less than 5 weight % trimers; alternatively,less than 4 weight % trimers; alternatively, less than 3 weight %trimers; 2 weight % trimers; alternatively, less than 1.75 weight %trimers; alternatively, less than 1.5 weight % trimers; alternatively,less than 1.25 weight % trimers; alternatively, less than 1 weight %trimers alternatively, less than 0.9 weight % trimers; alternatively,less than 0.8 weight % trimers; alternatively, less than 0.7 weight %trimers; alternatively, less than 0.6 weight % trimers; alternatively,less than 0.5 weight % trimers; alternatively, less than 0.4 weight %trimers alternatively, less than 0.3 weight % trimers; alternatively,less than 0.2 weight % trimers; or alternatively, less than 0.1 weight %trimers. In another aspect, the collection of alpha olefin monomer andalpha olefin product in the reactor effluent or the alpha olefin productaccording to this disclosure can comprise at least 50 weight % higheroligomers (containing 4 or more alpha olefin monomer units);alternatively, at least 55 weight % higher oligomers; alternatively, atleast 60 weight % higher oligomers; alternatively, at least 62.5 weight% higher oligomers; alternatively, at least 65 weight % higheroligomers; alternatively, at least 67.5 weight % higher oligomers;alternatively, at least 70 weight % higher oligomers; alternatively, atleast 72.5 weight % higher oligomers; alternatively, at least 75 weight% higher oligomers; alternatively, at least 77.5 weight % higheroligomers; alternatively, at least 80 weight % higher oligomers; atleast 82.5 weight % higher oligomers; alternatively, at least 85 weight% higher oligomers; alternatively, at least 86 weight % higheroligomers; alternatively, at least 87 weight % higher oligomers;alternatively, at least 88 weight % higher oligomers; alternatively, atleast 89 weight % higher oligomers; alternatively, at least 90 weight %higher oligomers; alternatively, at least 91 weight % higher oligomers;alternatively, at least 92 weight % higher oligomers; alternatively, atleast 93 weight % higher oligomers; alternatively, at least 94 weight %higher oligomers; or alternatively, at least 95 weight % higheroligomers. Moreover, any appropriate combination of these alpha olefinoligomer weight percentage features can be utilized to describe thecollection of alpha olefin monomer and alpha olefin product in thereactor effluent and/or the alpha olefin product. Generally, the weightpercent of alpha olefin monomers, dimers, trimers, and higher oligomersof the collection of alpha olefin monomer and alpha olefin product inthe reactor effluent satisfy the formula monomer+dimer+trimer+higheroligomer=100. Generally, the weight percent of dimers, trimers, andhigher oligomers of the alpha olefin polymerization (or oligomerization)product satisfy the formula dimers+trimers+higher oligomers=100.However, when desired or necessary for clarity, the amount of monomer(residual monomer) can be stated (e.g., when referring to a fractionatedreactor effluent, among other compositions) and in this instance theweight percent of alpha olefin monomers, dimers, trimers, and higheroligomers satisfy the formula monomers+dimers+trimers+higheroligomers=100.

In an aspect, the heavy oligomer product can comprise less than 1 weight% alpha olefin monomer, alternatively, less than 0.8 weight % alphaolefin monomer; alternatively, less than 0.6 weight % alpha olefinmonomer; alternatively, less than 0.5 weight % alpha olefin monomer,alternatively, less than 0.4 weight % alpha olefin monomeralternatively, less than 0.3 weight % alpha olefin monomer;alternatively, less than 0.2 weight % alpha olefin monomer; oralternatively, less than 0.1 weight % alpha olefin monomer. In someaspects, the alpha olefin monomer content of the heavy oligomer productcan be referred to as residual alpha olefin monomer and can utilize anyalpha olefin monomer content described herein. In another aspect, theheavy oligomer product according to this disclosure can comprise lessthan 10 weight % dimers; alternatively, less than 9 weight % dimers;alternatively, less than 8 weight % dimers; alternatively, less than 7weight % dimers; alternatively, less than 6 weight % dimers;alternatively, less than 5 weight % dimers; alternatively, less than 4.5weight % dimers; alternatively, less than 4 weight % dimers;alternatively, less than 3 weight % dimers; alternatively, less than 2.5weight % dimers; alternatively, less than 2 weight % dimers;alternatively, less than 1.75 weight % dimers; alternatively, less than1.5 weight % dimers; alternatively, less than 1.25 weight % dimers;alternatively, less than 1 weight % dimers; alternatively, less than 0.9weight % dimers; alternatively, less than 0.8 weight % dimers;alternatively, less than 0.7 weight % dimers; alternatively, less than0.6 weight % dimers; alternatively, less than 0.5 weight % dimers;alternatively, less than 0.4 weight % dimers; alternatively, less than0.3 weight % dimers; alternatively, less than 0.2 weight % dimers; oralternatively, less than 0.1 weight % dimers. In another aspect, theheavy oligomer product can comprise less than 20 weight % trimers;alternatively, less than 17.5 weight % trimers; alternatively, less than15 weight % trimers; alternatively, less than 12.5 weight % trimers;alternatively, less than 10 weight % trimers; less than 7.5 weight %trimers; alternatively, less than 5 weight % trimers; alternatively,less than 4 weight % trimers; alternatively, less than 3 weight %trimers; 2 weight % trimers; alternatively, less than 1.75 weight %trimers; alternatively, less than 1.5 weight % trimers; alternatively,less than 1.25 weight % trimers; alternatively, less than 1 weight %trimers; alternatively, less than 0.9 weight % trimers; alternatively,less than 0.8 weight % trimers; alternatively, less than 0.7 weight %trimers; alternatively, less than 0.6 weight % trimers; alternatively,less than 0.5 weight % trimers; alternatively, less than 0.4 weight %trimers; alternatively, less than 0.3 weight % trimers; alternatively,less than 0.2 weight % trimers; or alternatively, less than 0.1 weight %trimers. In yet another aspect, the heavy oligomer product can compriseat least 80 weight % higher oligomers; at least 82.5 weight % higheroligomers; alternatively, at least 85 weight % higher oligomers;alternatively, at least 86 weight % higher oligomers; alternatively, atleast 87 weight % higher oligomers; alternatively, at least 88 weight %higher oligomers; alternatively, at least 89 weight % higher oligomers;alternatively, at least 90 weight % higher oligomers; alternatively, atleast 91 weight % higher oligomers; alternatively, at least 92 weight %higher oligomers; alternatively, at least 93 weight % higher oligomers;alternatively, at least 94 weight % higher oligomers; or alternatively,at least 95 weight % higher oligomers. Moreover, any appropriatecombination of these weight percentage features can be utilized todescribe a heavy oligomer product as provided herein. Generally, theweight percent of alpha olefin monomer, dimers, trimers, and higheroligomers of the heavy oligomer product satisfy the formulamonomers+dimers+trimers+higher oligomers=100. In some instances, it maybe desired only to refer to the heavy oligomer composition in terms ofthe oligomers and in this instance the weight percent of dimers,trimers, and higher oligomers of the heavy oligomer product satisfy theformula dimers+trimers+higher oligomers=100.

In an aspect, the PAO provided according to this disclosure, cancomprise less than 1 weight % hydrogenated alpha olefin monomer;alternatively, less than 0.8 weight % hydrogenated alpha olefin monomer,alternatively, less than 0.6 weight % hydrogenated alpha olefin monomer,alternatively, less than 0.5 weight % hydrogenated alpha olefin monomer,alternatively, less than 0.4 weight % hydrogenated alpha olefin monomer,alternatively, less than 0.3 weight % hydrogenated alpha olefin monomer;alternatively, less than 0.2 weight % hydrogenated alpha olefin monomer,or alternatively, less than 0.1 weight % hydrogenated alpha olefinmonomer. In another aspect, the PAO prepared according to thisdisclosure can comprise less than 10 weight % hydrogenated dimers;alternatively, less than 9 weight % hydrogenated dimers; alternatively,less than 8 weight % hydrogenated dimers; alternatively, less than 7weight % hydrogenated dimers; alternatively, less than 6 weight %hydrogenated dimers; alternatively, less than 5 weight % hydrogenateddimers; alternatively, less than 4 weight % hydrogenated dimers;alternatively, less than 4.5 hydrogenated dimers; alternatively, lessthan 3.5 hydrogenated dimers; alternatively, less than 3 weight %hydrogenated dimers; less than 2.5 weight % hydrogenated dimers;alternatively, less than 2 weight % hydrogenated dimers; alternatively,less than 1.75 weight % hydrogenated dimers; alternatively, less than1.5 weight % hydrogenated dimers; alternatively, less than 1.25 weight %hydrogenated dimers; alternatively, less than 1 weight % hydrogenateddimers; alternatively, less than 0.9 weight % hydrogenated dimers;alternatively, less than 0.8 weight % hydrogenated dimers;alternatively, less than 0.7 weight % hydrogenated dimers;alternatively, less than 0.6 weight % hydrogenated dimers;alternatively, less than 0.5 weight % hydrogenated dimers;alternatively, less than 0.4 weight % hydrogenated dimers;alternatively, less than 0.3 weight % hydrogenated dimers;alternatively, less than 0.2 weight % hydrogenated dimers; oralternatively, less than 0.1 weight % hydrogenated dimers. In anotheraspect, the PAO according to this disclosure can comprise less than 20weight % hydrogenated trimers; alternatively, less than 17.5 weight %hydrogenated trimers; alternatively, less than 15 weight % hydrogenatedtrimers; alternatively, less than 12.5 weight % hydrogenated trimers;alternatively, less than 10 weight % hydrogenated trimers; less than 7.5weight % hydrogenated trimers; alternatively, less than 5 weight %hydrogenated trimers; alternatively, less than 4 weight % hydrogenatedtrimers; alternatively, less than 3 weight % hydrogenated trimers; 2weight % hydrogenated trimers; alternatively, less than 1.75 weight %hydrogenated trimers; alternatively, less than 1.5 weight % hydrogenatedtrimers; alternatively, less than 1.25 weight % hydrogenated trimers;alternatively, less than 1 weight % hydrogenated trimers; alternatively,less than 0.9 weight % hydrogenated trimers; alternatively, less than0.8 weight % hydrogenated trimers; alternatively, less than 0.7 weight %hydrogenated trimers; alternatively, less than 0.6 weight % hydrogenatedtrimers; alternatively, less than 0.5 weight % hydrogenated trimers;alternatively, less than 0.4 weight % hydrogenated trimers;alternatively, less than 0.3 weight % hydrogenated trimers;alternatively, less than 0.2 weight % hydrogenated trimers; oralternatively, less than 0.1 weight % hydrogenated trimers. In a furtheraspect, the PAO according to this disclosure can comprise at least 80weight % hydrogenated higher oligomers; at least 82.5 weight %hydrogenated higher oligomers; alternatively, at least 85 weight %hydrogenated higher oligomers; alternatively, at least 86 weight %hydrogenated higher oligomers; alternatively, at least 87 weight %hydrogenated higher oligomers; alternatively, at least 88 weight %hydrogenated higher oligomers; alternatively, at least 89 weight %hydrogenated higher oligomers; alternatively, at least 90 weight %hydrogenated higher oligomers; alternatively, at least 91 weight %hydrogenated higher oligomers; alternatively, at least 92 weight %hydrogenated higher oligomers; alternatively, at least 93 weight %hydrogenated higher oligomers; alternatively, at least 94 weight %hydrogenated higher oligomers; or alternatively, at least 95 weight %hydrogenated higher oligomers. Moreover, any appropriate combination ofthese features can be utilized to describe a PAO provided herein.Generally, the weight percent of hydrogenated alpha olefin monomers,hydrogenated dimers, hydrogenated trimers, and hydrogenated higheroligomers of the PAO satisfy the formula monomer+dimer+trimer+higheroligomer=100. In some instances, it may be desired only to refer to thePAO in terms of the oligomers, and in these instances, the weightpercent of hydrogenated dimers, hydrogenated trimers, and hydrogenatedhigher oligomers of the PAO satisfy the formula dimers+trimers+higheroligomers=100. When referring the PAO, hydrogenated monomers,hydrogenated dimers, hydrogenated trimers, and hydrogenated higherolefins can also be referenced as saturated monomers, saturated dimers,saturated trimers, and saturated higher oligomers (respectively) andthat any number associated with hydrogenated monomers, hydrogenateddimers, hydrogenated trimers, and hydrogenated higher olefins can beapplied to the respective saturated alternative.

In an embodiment consistent with this invention, a process for producinga product (e.g., an alpha olefin product, an oligomerization product,etc.) can comprise contacting a catalyst composition and an alpha olefinmonomer comprising a C₄ to C₆₀ alpha olefin to produce the product, andin this embodiment, the catalyst composition can comprise anN,N-bis[2-hydroxidebenzyl]amine compound having formula (IIa) and/or(IIIb), an activator-support, and optionally, a co-catalyst. Alphaolefin products thus produced often can have a M_(w) in a range fromabout 1,000 to about 150,000 g/mol. In some aspects, for instance, theM_(w) of the alpha olefin product can be at least 1,000; alternatively,at least 1,500; alternatively, at least 2,000; alternatively, at least2,500; alternatively, at least 3,000; alternatively, at least 3,500;alternatively, at least 4,000; alternatively, at least 4,500;alternatively, at least 5,000; alternatively, at least 5,500;alternatively, at least 6,000; alternatively, at least 6,500;alternatively, at least 7,000; alternatively, at least 7,500;alternatively, at least 8,000; alternatively, at least 8,500;alternatively, at least 9,000; alternatively, at least 9,500);alternatively, at least 10,000; alternatively, at least 11,000;alternatively, at least 12,000; alternatively, at least 13,000;alternatively, at least 14,000; alternatively, at least 15,000;alternatively, at least 16,000; alternatively, at least 17,000;alternatively, at least 18,000; alternatively, at least 19,000; oralternatively, at least 20,000 g/mol. In some aspects, the M_(w) of thealpha olefin product can have an upper limit of M_(w) of 150,000;alternatively, 140,000; alternatively, 130,000; alternatively, 120,000;alternatively 110,000; alternatively, 100,000; alternatively, 90,000;alternatively, 80,000; alternatively, 70,000; alternatively, 60,000;alternatively, 50,000; alternatively, 45,000; alternatively, 40,000;alternatively, 35,000; alternatively, 30,000; or alternatively, 25,000g/mol. In these and other aspects, the alpha olefin product can have aM, in a range from any minimum M_(w) disclosed herein to any maximumM_(w) disclosed herein. As non-limiting examples, the alpha olefinproduct can have a M_(w) in a range from 1,000 to 150,000;alternatively, from 2,000 to 150,000; alternatively, from 3,000 to100,000; alternatively, from 3,500 to 75,000; alternatively, from 4,000to 50,000; alternatively, from 3,000 to 40,000; alternatively, from3,000 to 30,000; or alternatively, from 5,000 to 25,000 g/mol. In afurther aspect, such molecular weights of the alpha olefin oligomerproduct can be achieved at an oligomerization temperature in a rangefrom 10° C. to 60° C., or in a range from 15° C. to 30° C., but notbeing limited thereto.

Embodiments of this invention are also directed to, and encompass, thealpha olefin polymer (or oligomer) products produced by any of thepolymerization (or oligomerization) processes disclosed herein. Articlesof manufacture can be formed from, and/or can comprise, the alpha olefinproducts produced in accordance with this invention. For instance, alubricant or lubricant composition can comprise an alpha olefin productproduced herein. In one aspect, the alpha olefin product can be aviscosity modifier in a lubricant composition. In another aspect, thealpha olefin product can be used as sole base oil or utilized incombination with another base oil (e.g., a mineral oil and/or a PAO).Additives that can be utilized with the alpha olefin product in variouscompositions can include, but are not limited to, metal deactivators,detergents, dispersants, antioxidants, and the like, or combinationsthereof.

In another embodiment consistent with this invention, a process forproducing a product (e.g., an alpha olefin product, a polymerizationproduct, etc.) can comprise contacting a catalyst composition and analpha olefin monomer comprising a C₄ to C₆₀ alpha olefin to produce theproduct, and in this embodiment, the catalyst composition can comprisean N,N-bis[2-hydroxidebenzyl]amine compound having formula (Ia) and/or(Ib), an activator-support, and optionally, a co-catalyst. Alpha olefinpolymer products thus produced often can have a M_(w) in a range fromabout 250,000 to about 750,000,000 g/mol. In some aspects, for instance,the M_(w) of the alpha olefin product can be at least 250,000;alternatively, at least 500,000; alternatively, at least 750,000;alternatively, at least 1,000,000; alternatively, at least 1,500,000;alternatively, at least 2,000,000; alternatively, at least 2,500,000;alternatively, at least 3,000,000; alternatively, at least 3,500,000; oralternatively, at least 4,000,000 g/mol. In some aspects, the M_(w) ofthe alpha olefin product can have an upper limit of M_(w) of750,000,000; alternatively, 500,000,000; alternatively, 250,000,000;alternatively, 100,000,000; alternatively, 75,000,000; alternatively,50,000,000; alternatively, 25,000,000; alternatively, 15,000,000;alternatively, 12,500,000; alternatively, 10,000,000; alternatively,7,500,000; or alternatively, 5,000,000 g/mol. In these and otheraspects, the alpha olefin product can have a M_(w) in a range from anyminimum M_(w) disclosed herein to any maximum M_(w) disclosed herein. Asnon-limiting examples, the alpha olefin product can have a M_(w) in arange from 250,000 to 750,000,000; alternatively, from 500,000 to250,000,000; alternatively, from 500,000 to 50,000,000; alternatively,from 750,000 to 50,000,000; alternatively, from 500,000 to 15,000,000;alternatively, from 1,000,000 to 10,000,000; alternatively, from 750,000to 7,500,000; alternatively, from 500,000 to 5,000,000; oralternatively, from 2,000,000 to 7,500,000 g/mol. In a further aspect,such molecular weights of the alpha olefin polymerization product can beachieved at a polymerization temperature in a range from 10° C. to 60°C., or in a range from 15° C. to 30° C., but not being limited thereto.

Embodiments of this invention are also directed to, and encompass, thealpha olefin polymer (or oligomer) products produced by any of thepolymerization (or oligomerization) processes disclosed herein. Articlesof manufacture can be formed from, and/or can comprise, the alpha olefinproducts produced in accordance with this invention. For instance, adrag reducing agent or a drag reducing composition can comprise an alphaolefin polymer product produced herein.

Polymerization/Oligomerization Processes

Catalyst compositions of the present invention can be used to polymerize(or oligomerize) alpha olefins to form polymer products (or oligomerproducts). One such process for producing an oligomer product cancomprise contacting a catalyst composition and an alpha olefin monomercomprising a C₄ to Ca alpha olefin to produce the product, wherein thecatalyst composition can comprise a transition metal compound havingformula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), anactivator-support, and an optional co-catalyst. Transition metalcomplexes having formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb)were discussed above.

In accordance with one aspect of the invention, the process can employ acatalyst composition comprising a transition metal compound havingformula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb) and anactivator-support. Activator-supports useful in the processes of thepresent invention were disclosed above. In another aspect, the catalystcomposition can further comprise one or more than one organoaluminumcompound or compounds (suitable organoaluminum compounds also werediscussed above). Thus, a process for producing an alpha olefin productcan employ a catalyst composition comprising a transition metal compoundhaving formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), anactivator-support, and an organoaluminum compound. In some aspects, theactivator-support can comprise (or consist essentially of, or consistof) fluorided alumina, chlorided alumina, bromided alumina, sulfatedalumina, fluorided silica-alumina, chlorided silica-alumina, bromidedsilica-alumina, sulfated silica-alumina, fluorided silica-zirconia,chlorided silica-zirconia, bromided silica-zirconia, sulfatedsilica-zirconia, fluorided silica-titania, fluorided silica-coatedalumina, sulfated silica-coated alumina, phosphated silica-coatedalumina, and the like, or combinations thereof. In some aspects, theorganoaluminum compound can comprise (or consist essentially of, orconsist of) trimethylaluminum, triethylaluminum, tri-n-propylaluminum,tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum,tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminumethoxide, diethylaluminum chloride, and the like, or combinationsthereof.

In accordance with another aspect of the invention, the process forproducing an alpha olefin product can employ a catalyst compositioncomprising a transition metal compound having formula (Ia), (Ib), (IIa),(IIb), (IIIa), and/or (IIIb), an activator-support, and an optionalco-catalyst, wherein the co-catalyst can comprise an aluminoxanecompound, an organoboron or organoborate compound, an ionizing ioniccompound, an organoaluminum compound, an organozinc compound, anorganomagnesium compound, or an organolithium compound, or anycombination thereof. Hence, aspects of this invention are directed to aprocess for producing an alpha olefin product, the process comprisingcontacting a catalyst composition and an alpha olefin monomer comprisinga C₄ to C₆₀ alpha olefin to produce the product, and the catalystcomposition can comprise a transition metal compound having formula(Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), an activator-support,and an aluminoxane compound; alternatively, a transition metal compoundhaving formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), anactivator-support, and an organoboron or organoborate compound;alternatively, a transition metal compound having formula (Ia), (Ib),(IIa), (IIb), (IIIa), and/or (IIIb), an activator-support, and anionizing ionic compound; alternatively, a transition metal compoundhaving formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), anactivator-support, and an organoaluminum compound; alternatively, atransition metal compound having formula (Ia), (Ib), (IIa), (IIb),(IIIa), and/or (IIIb), an activator-support, and an organozinc compound;alternatively, a transition metal compound having formula (Ia), (Ib),(IIa), (IIb), (IIIa), and/or (IIIb), an activator-support, and anorganomagnesium compound; or alternatively, a transition metal compoundhaving formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), anactivator-support, and an organolithium compound. Furthermore, more thanone co-catalyst can be employed, e.g., an organoaluminum compound and analuminoxane compound, an organoaluminum compound and an ionizing ioniccompound, etc.

In accordance with yet another aspect of the invention, a process forproducing an alpha olefin polymerization product can comprise contactinga catalyst composition and an alpha olefin monomer comprising a C₄ toC₆₀ alpha olefin to produce the alpha olefin polymerization product. Inthis aspect, the process can be conducted at a temperature of greaterthan 10° C. (or in a range from 15° C. to 50° C.), the M_(w) of thepolymerization product can be greater than about 2,000,000 g/mol (or ina range from about 2,500,000 to about 10,000,000 g/mol), and thecatalyst composition can comprise an activator-support (e.g., fluoridedalumina, chlorided alumina, bromided alumina, sulfated alumina,fluorided silica-alumina, chlorided silica-alumina, bromidedsilica-alumina, sulfated silica-alumina, fluorided silica-zirconia,chlorided silica-zirconia, bromided silica-zirconia, sulfatedsilica-zirconia, fluorided silica-titania, fluorided silica-coatedalumina, sulfated silica-coated alumina, phosphated silica-coatedalumina, and the like, or combinations thereof). The catalystcomposition can comprise a transition metal compound, such as thosehaving formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or (IIIb), but notlimited thereto. For instance, the catalyst composition can comprise anactivator-support and a metallocene compound (e.g., a bridgedmetallocene compound, an unbridged metallocene compound, etc.).

In one aspect, the process for producing alpha olefin products accordingto this disclosure involves contacting at least one alpha olefin monomerwith a catalyst system to form the alpha olefin product. The reactoreffluent that is contained in the reactor following the process, whichcontains the alpha olefin product and typically some residual monomer(along with other components—e.g., catalyst system or catalyst systemcomponents), can be subjected to a separation process to remove some ofthe more volatile components from the reactor effluent, to provide aheavy oligomer product. The heavy oligomer product can then be subjectedto hydrogenation to form a polyalphaolefin (PAO). In some non-limitingaspects, the reactor effluent can be treated with an agent to deactivatethe system (a deactivation agent) before performing the separation. Forexample, the deactivation agent can comprise, consist essentially of, orconsist of, water, an alcohol, or any combination thereof;alternatively, water, or alternatively, an alcohol.

In an aspect, the present disclosure relates to a process for producingan alpha olefin product comprising contacting a catalyst composition andan alpha olefin monomer comprising a C₄ to C₆₀ alpha olefin to producethe product, wherein the catalyst composition can comprise a transitionmetal compound having formula (Ia), (Ib), (IIa), (IIb), (IIIa), and/or(IIIb), an activator-support, and an optional co-catalyst. In anotheraspect, the process can further comprise a step of separating a reactoreffluent comprising the alpha olefin product to provide a heavy oligomerproduct. In yet another aspect, the process can further comprisehydrogenating the heavy oligomer product to provide a polyalphaolefin.In some aspects, the alpha olefin product can be recovered;alternatively, the heavy oligomer product can be recovered;alternatively, the hydrogenated heavy oligomer product can be recovered;or alternatively, the polyalphaolefin can be recovered.

In an aspect, the alpha olefin monomer utilized in the disclosedprocesses can comprise, or consist essentially of, a C₆ to C₁₄ normalalpha olefin; alternatively, a C₆ normal alpha olefin, a C₈ normal alphaolefin, a C₁₀ normal alpha olefin, a C₁₂ normal alpha olefin, a C₁₄normal alpha olefin, or any combination thereof; or alternatively, a C₈normal alpha olefin, a C₁₀ normal alpha olefin, a C₁₂ normal alphaolefin, or any combination thereof. Other alpha olefin monomers aredisclosed herein and can be utilized, without limitation, within theprocesses described herein.

In an aspect, the oligomerization/polymerization conditions utilized inthe processes for producing an alpha olefin oligomer/polymer cancomprise a reaction temperature in range from −20° C. to 150° C.;alternatively, from 0° C. to 140° C.; alternatively, from 0° C. to 125°C.; alternatively, from 5° C. to 100° C.; alternatively, from 5° C. to90° C.; or alternatively, from 10° C. to 80° C. In another aspect, thereaction temperature can be in a range from 10° C. to 60° C., while inyet another aspect, the reaction temperature can be in a range from 15°C. to 50° C., or from 15° C. to 30° C.

In an aspect, the disclosed processes for producing an alpha olefinproduct can be conducted in an inert atmosphere. In one aspect, an inertatmosphere is an atmosphere substantially free of oxygen; alternatively,substantially free of water when the reaction begins; or alternatively,substantially free of oxygen and substantially free of water when thereaction begins. In another aspect, the amount of water can be less than100 ppm; alternatively, less than 75 ppm; alternatively, less than 50ppm; alternatively, less than 30 ppm; alternatively, less than 25 ppm;alternatively, less than 20 ppm; alternatively, less than 15 ppm;alternatively, less than 10 ppm; alternatively, less than 5 ppm;alternatively, less than 3 ppm; alternatively, less than 2 ppm;alternatively, less than 1 ppm; or alternatively, less than 0.5 ppm. Inyet another aspect, the amount of oxygen can be less than 100 ppm;alternatively, less than 75 ppm; alternatively, less than 50 ppm;alternatively, less than 30 ppm; alternatively, less than 25 ppm;alternatively, less than 20 ppm; alternatively, less than 15 ppm;alternatively, less than 10 ppm; alternatively, less than 5 ppm;alternatively, less than 3 ppm; alternatively, less than 2 ppm;alternatively, less than 1 ppm; or alternatively, less than 0.5 ppm. Instill another aspect, the inert atmosphere can be dry nitrogen, oralternatively, dry argon.

In an aspect, the disclosed processes for producing an alpha olefinproduct can be conducted in the substantial absence of ethylene. Forexample, the process can be conducted with a partial pressure ofethylene of less than 10 psig; alternatively, less than 7 psig;alternatively, less than 5 psig; alternatively, less than 4 psig,alternatively, less than 3 psig; alternatively, less than 2 psig; oralternatively, less than 1 psig.

In an aspect, the disclosed processes for producing an alpha olefinproduct can be conducted in the substantial absence of hydrogen. Thiscan include, but is not limited to, a partial pressure of hydrogen ofless than 10 psig; alternatively, less than 7 psig; alternatively, lessthan 5 psig; alternatively, less than 4 psig; alternatively, less than 3psig; alternatively, less than 2 psig; or alternatively, less than 1psig.

However, in some aspects, the oligomerization/polymerization can beconducted in the presence of hydrogen. In these aspects, the hydrogenpartial pressure can be any pressure of hydrogen that does not adverselyaffect the oligomerization/polymerization reaction. While not intendingto be bound by theory, hydrogen can be used control the molecular weightof the product. In one aspect, the partial pressure of hydrogen duringoligomerization/polymerization is greater than or equal to 5 psig;alternatively, greater than or equal to 10 psig; alternatively, greaterthan or equal to 50 psig; alternatively, greater than or equal to 100psig; alternatively, greater than or equal to 200 psig; alternatively,greater than or equal to 300 psig; alternatively, greater than or equalto 400 psig; alternatively, greater than or equal to 500 psig;alternatively, greater than or equal to 750 psig; alternatively, greaterthan or equal to 1000 psig; alternatively, greater than or equal to 1250psig; or alternatively, greater than or equal to 1500 psig. In anotheraspect, the partial pressure of hydrogen can be in a range from 0 psigto 2000 psig; alternatively, from 1 psig to 1500 psig; alternatively,from 5 psig to 1250 psig; alternatively, from 10 psig to 1000 psig;alternatively, from 50 psig to 750 psig; alternatively, from 100 psig to500 psig; alternatively, from 150 psig to 400 psig; or alternatively,from 200 psig to 300 psig.

In accordance with a further aspect of this disclosure, the yield of thealpha olefin product is at least 25 weight % (i.e., 25 weight % of thealpha olefin monomer has been converted to the alpha olefinoligomer/polymer); alternatively, at least 30 weight %; alternatively,at least 35 weight %; alternatively, at least 40 weight %;alternatively, at least 45 weight %; alternatively, at least 50 weight%; or alternatively, at least 55 weight %. Such yields can be achievedat a reaction temperature in a range from 15° C. to 30° C. (e.g.,approximately 25° C.), and a reaction time in a range from 12 to 36hours (e.g., 24 hours). Additionally, these yields can be achieved at analpha olefin monomer:transition metal compound weight ratio of greaterthan 1500:1, greater than 1750:1, or greater than 2000:1.

In an aspect, the separation process or system utilized to remove atleast a portion of the monomer, dimer, and/or trimer from a(polymerization or oligomerization) reactor effluent to form a heavyoligomer product can be any separation process or system capable ofseparating at least a portion of the monomer, dimer, and/or trimer fromthe reactor effluent. In a non-limiting aspect, the separation processcan comprise distillation. In another aspect, the separation cancomprise wiped film evaporation. In some aspects, the distillation orwiped film evaporation can be performed at a pressure less than 760 torralternatively, less than 600 torr, alternatively, less than 400 torr;alternatively, less than 200 torr; alternatively, less than 100 torralternatively, less than 75 torr alternatively, less than 50 torr;alternatively, less than 40 torr, alternatively, less than 30 torralternatively, less than 20 torr; alternatively, less 10 torr;alternatively, less than 5 torr or alternatively, less than 1 torr.Moreover, the distillation or wiped film evaporation can be performed bysparging a gas through the distillation equipment or wiped filmevaporator. In some aspects, the sparging gas can be an inert gas, suchas nitrogen, helium, argon, or combinations thereof; alternatively,nitrogen; alternatively, helium, or alternatively argon.

The processes for producing an alpha olefin product (and optionally,separating a reactor effluent comprising the alpha olefin product toprovide a heavy oligomer product, and hydrogenating the heavy oligomerproduct to provide a polyalphaolefin) can be carried out in the absenceof a diluent; or alternatively, can be performed using a diluent, orsolvent. Solvents which can be utilized in theses processes can include,but are not limited to, aliphatic hydrocarbons, aromatic hydrocarbons,halogenated aliphatic hydrocarbons, halogenated aromatic hydrocarbons,and combinations thereof; alternatively, aliphatic hydrocarbons;alternatively, aromatic hydrocarbons; alternatively, halogenatedaliphatic hydrocarbons; or alternatively, halogenated aromatichydrocarbons. Aliphatic hydrocarbons which can be useful as a solventinclude C₃ to C₂₀ aliphatic hydrocarbons; alternatively, C₃ to C₁₅aliphatic hydrocarbons; or alternatively, C₄ to C₁₀ aliphatichydrocarbons. The aliphatic hydrocarbons can be cyclic or acyclic and/orcan be linear or branched, unless otherwise specified. Non-limitingexamples of suitable acyclic aliphatic hydrocarbon solvents that can beutilized singly or in any combination include propane, iso-butane,butane, pentane (n-pentane or mixture of linear and branched C₅ acyclicaliphatic hydrocarbons), hexane (n-hexane or mixture of linear andbranched C₆ acyclic aliphatic hydrocarbons), heptane (n-heptane ormixture of linear and branched C₇ acyclic aliphatic hydrocarbons),octane, and combinations thereof. Non-limiting examples of suitablecyclic aliphatic hydrocarbon solvents include cyclohexane and methylcyclohexane. Aromatic hydrocarbons which can be useful as a solventinclude C₆ to C₂₀ aromatic hydrocarbons, or alternatively, C₆ to C₁₀aromatic hydrocarbons. Non-limiting examples of suitable aromatichydrocarbons that can be utilized singly or in any combination includebenzene, toluene, xylene (including ortho-xylene, meta-xylene,para-xylene, or mixtures thereof), and ethylbenzene, or combinationsthereof. Halogenated aliphatic hydrocarbons which can be useful as asolvent include C₁ to C₁₅ halogenated aliphatic hydrocarbons;alternatively, C₁ to C₁₀ halogenated aliphatic hydrocarbons; oralternatively, C₁ to C₅ halogenated aliphatic hydrocarbons. Thehalogenated aliphatic hydrocarbons can be cyclic or acyclic and/or canbe linear or branched, unless otherwise specified. Non-limiting examplesof suitable halogenated aliphatic hydrocarbons which can be utilizedsingly of in any combination include methylene chloride, carbontetrachloride, dichloroethane, trichloroethane, and combinationsthereof. Halogenated aromatic hydrocarbons which can be useful as asolvent include C₆ to C₂₀ halogenated aromatic hydrocarbons, oralternatively, C₅ to C₁₀ halogenated aromatic hydrocarbons. Non-limitingexamples of suitable halogenated aromatic hydrocarbons that can beutilized singly or in any combination include chlorobenzene,dichlorobenzene, and combinations thereof.

Alpha olefin polymerization/oligomerization according to this disclosurecan be carried out in any manner known in the art suitable for thespecific alpha olefin monomer(s) employed in the process. For example,processes can include, but are not limited to slurry processes, solutionprocesses, and the like, including multi-reactor combinations thereof.For example, a stirred reactor can be utilized for a batch process, orthe reaction can be carried out continuously in a loop reactor or in acontinuous stirred reactor. Slurry processes (also known as the particleform process) are well known in the art and are disclosed, for examplein U.S. Pat. No. 3,248,179, which is incorporated by reference herein inits entirety. Other contemplated methods of the present disclosure forslurry processes are those employing a loop reactor of the typedisclosed in U.S. Pat. No. 3,248,179, and those utilized in a pluralityof stirred reactors either in series, parallel, or combinations thereof,wherein the reaction conditions are different in the different reactors

Polymerization/oligomerization reactors and reactor systems can includeany polymerization/oligomerization reactor or reactor system known inthe art that is capable of polymerizing/oligomerizing an alpha olefinmonomer to produce an alpha olefin polymer/oligomer product according tothe present disclosure. Such systems can comprise at least one rawmaterial feed system, at least one feed system for the catalyst systemor catalyst system components, at least one reactor system, at least oneproduct recovery system, or any suitable combination thereof. Suitablereactors for the present disclosure can further comprise any one, orcombination of, a catalyst system storage system, catalyst systemcomponent storage system, a cooling system, a diluent or solventrecycling system, a monomer recycling system, or a control system. Suchreactors can comprise continuous take-off and direct recycling ofcatalyst, diluent, monomer, and alpha olefin product. Generally,continuous processes can comprise the continuous introduction of analpha olefin monomer, a catalyst composition, and a diluent into areactor and the continuous removal from this reactor of a suspensioncomprising alpha olefin product, catalyst composition, and the diluentor solvent(s).

Reactor systems of the present disclosure can comprise one type ofreactor per system or multiple reactor systems comprising two or moretypes of reactors operated in parallel or in series. Multiple reactorsystems can comprise reactors connected together to perform thereaction, or reactors that are not connected. The alpha olefin monomercan be polymerized/oligomerized in one reactor under one set ofconditions, and then this material comprising an alpha olefinintermediate polymer/oligomer (and potentially the catalyst systemand/or unreacted alpha olefin monomer of this first reactor) can betransferred to a second reactor for polymerization/oligomerization undera different set of conditions.

In one aspect of the disclosure, the reactor system can comprise atleast one loop reactor. Such reactors are known in the art and cancomprise vertical or horizontal loops. Such loops can comprise a singleloop or a series of loops. Multiple loop reactors can comprise bothvertical and horizontal loops. The process can be performed using thealpha olefin monomer as the liquid carrier, or in the presence of anorganic diluent or solvent that can disperse and/or carry the catalystsystem components and/or catalyst system. An organic solvent can also beutilized to reduce the viscosity of the reaction mixture (including thealpha olefin product) and allow the reaction mixture to easily flow orbe pumped through the process equipment. Suitable solvents are disclosedherein. Monomer(s), solvent, catalyst system components and/or catalystsystem, can be continuously fed to a loop reactor wherepolymerization/oligomerization occurs.

In still another aspect of the disclosure, the reactor system cancomprise a tubular reactor. Tubular reactors can have several zoneswhere fresh monomer, the catalyst system, and/or catalyst systemcomponents (and/or other components of the reaction, e.g., hydrogen) areadded. Monomer can be introduced at one zone of the reactor while thecatalyst system, and/or catalyst components (and/or other components ofthe reaction, e.g., hydrogen) can be introduced at another zone of thereactor. Heat and pressure can be employed appropriately to obtainoptimal reaction conditions.

In another aspect of the disclosure, the reactor system can comprise asolution reactor. In a solution process, the alpha olefin monomer can becontacted with the catalyst system and/or catalyst system components bysuitable stirring or other means. A carrier comprising an inert organicdiluent (if employed) or excess monomer can be employed. If desired, themonomer can be brought in the vapor phase into contact with thecatalytic reaction product, in the presence or absence of liquidmaterial. The reaction zone is maintained at temperatures and pressuresthat will result in the formation of a solution of the alpha olefinproduct in a reaction medium. Agitation can be employed during thereaction to obtain better temperature control and to maintain uniformreaction component mixtures throughout the reaction zone. Adequate meansare utilized for dissipating the exothermic heat ofpolymerization/oligomerization. The process can be performed in a batchmanner or in a continuous manner. The reactor can comprise a series ofat least one separator that employs high pressure and/or low pressure toseparate the desired alpha olefin product.

In a further aspect of the disclosure, the reactor system can comprisethe combination of two or more reactors. Production of alpha olefinproducts in multiple reactors can include several stages in at least twoseparate reactors interconnected by a transfer device making it possibleto transfer an intermediate product resulting from the first reactorinto the second reactor. The desired reaction conditions in one of thereactors can be different from the operating conditions of the otherreactors. Alternatively, a multiple reactor system can include themanual transfer of an intermediate product from one reactor tosubsequent reactors for continued polymerization/oligomerization. Suchreactors can include, but not limited to, any combination of one or moreloop reactors, one or more tubular reactors, one or more solutionreactors, one or more stirred tank reactors, or one or more autoclavereactors.

In an aspect, the process can include a separation step or multipleseparation steps to remove or at least a portion of unreacted monomer,dimer, and/or trimers. In an aspect, the separation step(s) are operatedto reduce the amount of monomer, dimer, and/or trimer found in thereactor effluent and/or alpha olefin product. Desirable monomer, dimer,and/or trimer contents are described herein and can be utilized withoutlimitation to further describe the separation step(s). The separationstep(s) can also be utilized to remove the diluent or solvent, ifutilized, from the alpha olefin product.

In some aspects, suitable additives and modifiers can be added to thealpha olefin oligomer product and/or the subsequent polyalphaolefin inorder to provide desired end-use properties or effects.

EXAMPLES

The invention is further illustrated by the following examples, whichare not to be construed in any way as imposing limitations to the scopeof this invention. Various other aspects, embodiments, modifications,and equivalents thereof which, after reading the description herein, maysuggest themselves to one of ordinary skill in the art without departingfrom the spirit of the present invention or the scope of the appendedclaims.

Unless otherwise noted, all operations were performed under purifiednitrogen or vacuum using standard Schlenk or glovebox techniques. Et₂O,THF, and N,N-dimethylformamide were obtained as anhydrous fromSigma-Aldrich and used as received. Pentane, hexanes, heptanes, andtoluene (obtained from Fischer Scientific) were degassed and stored overactivated 13X molecular sieves under nitrogen. 1 M triisobutylaluminum(TIBA) in hexanes, 10% MAO in toluene, 2,4-di-tert-butylphenol, lithiumhydroxide hydrate, paraformaldehyde, thionyl chloride, allyl amine,3-butenylamine, and formaldehyde were obtained from Sigma-Aldrich andused as received. (B(C₆F₅)₃) and [Ph₃C][B(C₆F₅)₄] were obtained fromBoulder Scientific Company, and ZrBn₄ and HfBn₄ were obtained from StremChemicals, Inc. C₆D₆ and d₁₂-cyclohexane (obtained from CambridgeIsotope Laboratories, Inc.) were degassed and dried over 13X molecularsieves under nitrogen. CDCl₃ (obtained from Cambridge IsotopeLaboratories, Inc.) was used as received.2-phenol-3,5-di-tert-butylbenzyl alcohol, NMe₂, OMe, TM-3, TM-A, andTM-C were prepared according to suitable synthesis procedures. The aminebis(phenolate) transition metal compounds TM-3, TM-A, and TM-C wereprepared generally as described in U.S. Pat. Nos. 6,333,423 and6,596,827, the disclosures of which are incorporated herein by referencein their entirety. Chemical shifts (δ) for ¹H NMR spectra are givenrelative to residual protium in the deuterated solvent at 7.27 and 7.16for C₆D₆ and CDCl₃, respectively.

Approximately 20% MAO on SiO₂ was prepared as follows. 17 grains ofGrade 952 SiO₂ from W.R. Grace & Company were charged to a 500-mLround-bottomed flask equipped with stirbar. A 10%/o MAO solution intoluene (57 mL) was added, resulting in a yellowish slurry. Pentane (500mL) was added to the slurry and the solution was cooled to −20° C.overnight. The suspension was filtered and dried in vacuo.

Fluorided silica-alumina activator-supports were prepared as follows. Asilica-alumina was obtained from W.R. Grace & Company containing about13% alumina by weight and having a surface area of about 400 m²/g and apore volume of about 1.2 mL/g. This material was obtained as a powderhaving an average particle size of about 70 microns. Approximately 100grams of this material were impregnated with a solution containing about200 mL of water and about 10 grams of ammonium hydrogen fluoride,resulting in a damp powder having the consistency of wet sand. Thismixture was then placed in a flat pan and allowed to dry under vacuum atapproximately 110° C. for about 16 hours. To calcine the support, about10 grams of this powdered mixture were placed in a 1.75-inch quartz tubefitted with a sintered quartz disk at the bottom. While the powder wassupported on the disk, air (nitrogen can be substituted) dried bypassing through a 13X molecular sieve column, was blown upward throughthe disk at the linear rate of about 1.6 to 1.8 standard cubic feet perhour. An electric furnace around the quartz tube was then turned on andthe temperature was raised at the rate of about 400° C. per hour to thedesired calcining temperature of about 450° C. At this temperature, thepowder was allowed to fluidize for about three hours in the dry air.Afterward, the fluorided silica-alumina (abbreviated “AS3” in the tablesthat follow) was collected and stored under dry nitrogen, and was usedwithout exposure to the atmosphere.

Fluorided silica-coated alumina activator-supports were prepared asfollows. A silica-coated alumina was obtained from Sasol Company underthe Siral® 28M designation. Approximately 65 g of ammonium bifluoridewere dissolved in 2.3 L of methanol, and this methanol solution wasadded to 650 g of Siral® 28M in a 4-L beaker while stirring. This wetmixture was then allowed to dry under vacuum at approximately 100° C.for about 16 hours. To calcine the resultant powdered mixture, a portionof the material was fluidized in a stream of dry nitrogen at about 600°C. for about 3 hours. Afterward, the fluorided silica-coated alumina(abbreviated “AS2” in the tables that follow) was collected and storedunder dry nitrogen, and was used without exposure to the atmosphere.

Sulfated alumina activator-supports were prepared as follows. Bohemitewas obtained from W.R. Grace & Company under the designation “Alumina A”and having a surface area of about 300 m²/g and a pore volume of about1.3 mL/g. This material was obtained as a powder having an averageparticle size of about 100 microns. This material was impregnated toincipient wetness with an aqueous solution of ammonium sulfate to equalabout 15% sulfate. This mixture was then placed in a flat pan andallowed to dry under vacuum at approximately 110° C. for about 16 hours.To calcine the resultant powdered mixture, the material was fluidized ina stream of dry air at about 550° C. for about 6 hours. Afterward, thesulfated alumina (abbreviated “AS1” in the tables that follow) wascollected and stored under dry nitrogen, and was used without exposureto the atmosphere.

Molecular weights and molecular weight distributions were obtained usinga PL-220 high temperature GPC/SEC unit (Polymer Laboratories, now anAgilent Company) with 1,2,4-trichlorobenzene (TCB) as the solvent, witha flow rate of 1 mL/min at a column temperature of 145° C.2,6-di-tert-butyl-4-methylphenol (BHT) at a concentration of 0.5 g/L wasadded to TCB as a stabilizer. An injection volume of 400 μL was usedwith a nominal polymer concentration of 1.5 mg/mL. Dissolution of thesample in stabilized TCB was carried out by heating at 150° C. for 5hours or longer, depending on sample, with occasional, gentle agitation.Three Waters 7.8 mm×300 mm Styragel HMW-6E columns were used. Thecolumns were calibrated with the broad calibration method using a broadlinear polyethylene standard (Chevron Phillips Chemical Company LPMarlex® BHB 5003) whose molecular weight and molecular weightdistribution had been determined independently. Mn is the number-averagemolecular weight (g/mol); M_(w) is the weight-average molecular weight(g/mol); M_(z) is the z-average molecular weight (g/mol); and PDI is thepolydispersity index, the ratio of M_(w)/M_(n). The Mark-Houwinkconstants, K and α, used for alpha olefin oligomer products were 5.19E-5dL/g and 0.77, respectively.

Example 1 Synthesis of 2-phenol-3,5-di-tert-butylbenzyl chloride

Approximately 20 mL of methylene chloride were added to2-phenol-3,5-di-tert-butylbenzyl alcohol (3.55 g, 15 mmol) in a 100 mLround-bottomed flask equipped with a stirbar. Thionyl chloride (1.28 ml,17.5 mmol) was added dropwise to the flask, yielding a yellow solutionwhich was stirred for 30 min. While stirring, a small amount of solidformed and was filtered off. Evacuation of the volatiles produced2-phenol-3,5-di-tert-butylbenzyl chloride as a pale yellow solid. ¹H NMR(CDCl₃): δ 7.36 (d, J=3.2 Hz, 1H), δ 7.10 (d, J=3.2 Hz, 1H), δ 5.41 (s,J=1.5, 1H, OH), δ 4.73 (s, 2H), δ 1.47 (s, 9H), δ 1.34 (s, 9H).

Examples 2-6 Synthesis of N,N-bis[2-hydroxidebenyl]amine compounds TM-1and TM-2

A representative general synthesis scheme for compounds TM-1 and TM-2 isillustrated below:

Ligand 1 was produced in Example 2. Approximately 25 mL ofN,N-dimethylformamide were added to 2-phenol-3,5-di-tert-butylbenzylchloride (1.0 g, 3.9 mmol) in a 100 mL round-bottomed flask equippedwith a stirbar. Under nitrogen flow, allylamine (0.15 mL, 2 mmol) andK₂CO₃ (1.62 g, 11.8 mmol) were added to the flask, and the resultingsuspension was stirred at ambient temperature for 72 hr. The reactionmixture was partitioned between 50 mL of a 1:1 NH₄Cl(sat):water mixtureand Et₂O (75 mL). The organics were separated and washed with water(2×50 mL) and brine (25 mL). The volatiles were evacuated leaving acolorless residue. The colorless crystals were isolated from a saturatedMeCN solution of Ligand 1 at −30° C. ¹H NMR (CDCl₃): δ 7.80 (s, 2H, OH),δ 7.25 (s, 2H), δ 6.94 (s, 1H), δ 6.01 (mult, 1H), δ 5.34 (m, 2H), δ3.72 (s, 4H), δ 3.19 (d, J=6.3 Hz, 2H), δ 1.45 (s, 18H), δ 1.32 (s,18H).

Ligand 1 was produced via an alternative procedure in Example 3.Approximately 10 mL of MeOH were added to 2,4-di-tert-butylphenol (5 g,24.2 mmol) in a 50 mL round-bottomed flask equipped with a stirbar.Formaldehyde (3 mL, 36 mmol) was added to the flask, then allylamine(0.91 mL, 12.1 mmol) by syringe. The resultant yellow solution washeated to reflux for 72 hr. Next, the reaction mixture was cooled toambient temperature, then to −30° C. for several hours. The biphasicsolution was decanted, and a thick oil was crystallized from a saturatedMeCN solution at −30° C., resulting in Ligand 1.

Ligand 2 was produced in Example 4. Approximately 75 mL ofN,N-dimethylformamide were added to 2-phenol-3,5-di-tert-butylbenzylchloride (3 g, 3.9 mmol) and 3-butenylamine (0.633 g, 5.89 mmol) in a200 mL round-bottomed flask equipped with a stirbar. Under nitrogenflow, K₂CO (5.7 g, 41.2 mmol) was added to the flask, and the resultingsuspension was stirred at ambient temperature for 72 hr. The reactionmixture was partitioned between 150 mL of a 1:1 NH₄Cl(sat):water mixtureand Et₂O (150 mL). The volatiles were evacuated leaving a pale yellowresidue. The pale yellow crystals were isolated from a saturated MeCNsolution of Ligand 2 at −30° C. ¹H NMR (CDCl₁): δ 7.69 (Is, 2H, OH), δ7.23 (d, J=2.1 Hz, 2H), δ 6.93 (d, J=2.1 Hz, 2H), δ 5.75 (mult, 1H), δ5.14 (m, 2H), δ 3.68 (s, 4H), δ 2.66 (t, J=6.6 Hz, 2H) δ 2.42 (q, J=6.6Hz, 2H), δ 1.44 (s, 18H), δ 1.31 (s, 18H).

Compound TM-1 was produced in Example 5. ZrBn₄ (0.4 g, 0.81 mmol) andLigand 1 (0.369 g, 0.81 mmol) were dissolved in 10 mL of PhMe. Thesolution was heated to 65° C. for 2 hr. The volatiles were removed,leaving a colorless solid which was crystallized from a saturatedpentane solution at −30° C., resulting in TM-1 and colorless crystals.¹H NMR (C₆D₆): δ 7.76 (d, J=8.4 Hz, 2H), δ 7.60 (d, J=2.4 Hz, 2H), δ7.28 (t, J=7.5 Hz, 2H), δ 7.1 (t, 1H), δ 6.93 (d, J=2.1 Hz, 2H), δ 6.90(d, J=8.4 Hz, 2H), δ 6.73 (t, J=7.2 Hz, 2H), δ 6.61 (t, J=7.2 Hz, 1H), δ5.33 (mult, 1H), δ 4.87 (dd, J=2.1, 10.2 Hz, 2H), δ 4.65 (dd, J=1.5,16.8 Hz, 2H), δ 3.32 (d, J=13.8 Hz, 2H), δ 2.94 (d, J=13.8 Hz, 2H), δ2.94 (s, 2H, ZrCH₂Ph), δ 2.72 (d, J=7.2 Hz, 2H), δ 1.98 (s, 2H,ZrCH₂Ph), δ 1.83 (s, 18H), δ 1.38 (s, 18H).

Compound TM-2 was produced in Example 6. ZrBn₄ (0.305 g, 0.6 mmol) andLigand 2 (0.273 g, 0.6 mmol) were dissolved in 10 mL of PhMe. Thesolution was heated to 65° C. for 2 hr. The volatiles were removed,leaving a colorless solid which was crystallized from a saturatedpentane solution at −30° C., resulting in TM-2 and colorless crystals.FIG. 3 illustrates the ¹H-NMR analysis of TM-2. ¹H NMR (C₆D₆): δ 7.77(d, J=8.4 Hz, 2H), δ 7.59 (d, J=2.4 Hz, 2H), δ 7.30 (t, J=7.5 Hz, 2H), δ7.14 (t, J=7.2 Hz, 1H), δ 6.98 (d, J=2.4 Hz, 2H), δ 6.93 (d, J=6.9 Hz,2H), δ 6.75 (t, J=7.5 Hz, 2H), δ 6.63 (t, J=7.5 Hz, 1H), δ 4.7-4.8(mult, 1H), δ 4.5-4.6 (mult, 2H), δ 3.36 (d, J=14.1 Hz, 2H), δ 3.02 (d,J=13.8 Hz, 2H), δ 3.01 (s, 2H, ZrCH₂Ph), δ 2.21 (t, J=7.8 Hz, 2H), δ1.96 (s, 2H, ZrCH₂Ph), δ 1.86 (q, J=6.6 Hz, 2H), δ 1.80 (s, 18H), δ 1.40(s, 18H).

Examples 7-8 Synthesis of Hafnium Analogs of Compounds TM-1 and TM-2

The hafnium analog of compound TM-1 was produced in Example 7. HfBn₄(0.11 g, 0.203 mmol) and Ligand 1 (0.1 g, 0.203 mmol) were dissolved in4 mL of PhMe. The solution was allowed to stand at ambient temperatureovernight. The volatiles were removed, resulting in a pale yellow solidof the hafnium analog of TM-1. ¹H NMR (C₆D₆): δ 7.70 (d, J=7.2 Hz, 2H),δ 7.66 (d, J=2.4 Hz, 2H), δ 7.20 (t, J=7.6 Hz, 2H), δ 7.05 (t, 7.6 Hz,1H), δ 7.0 (d, 2H), δ 6.90 (d, J=2.4 Hz, 2H), δ 6.72 (t, J=7.6 Hz, 2H),δ 6.59 (t, J=7.6 Hz, 1H), δ 5.20 (mult, 1H), δ 4.82 (dd, J=1.6, 10 Hz,2H), δ 4.64 (dd, J=1.6, 17.2 Hz, 2H), δ 3.18 (d, J=14 Hz, 2H), δ 2.85(d, J=14 Hz, 2H), δ 2.76 (s, 2H, HfCH₂Ph), δ 2.47 (d, J=7.6 Hz, 2H), δ2.24 (s, 2H, HfCH₂Ph), δ 1.80 (s, 18H), δ 1.35 (s, 18H).

The hafnium analog of compound TM-2 was produced in Example 8. HfBn₄(0.107 g, 0.197 mmol) and Ligand 2 (0.1 g, 0.197 mmol) were dissolved in4 mL of PhMe. The solution was allowed to stand at ambient temperatureovernight. The volatiles were removed, resulting in a pale yellow gummysolid of the hafnium analog of TM-2 with impurities.

Examples 9-53 Alpha-Olefin Polymerization Experiments UsingN,N-bis[2-hydroxidebenzyl]amine Compounds

Polymerization experiments were conducted as follows. For catalystcompositions containing MAO or the organoboron compound, the catalystcomponents were charged to a vial equipped with a stirbar. At roomtemperature of approximately 25° C., the α-olefin (e.g., 1-hexene,1-octene) was added while stirring, and the reaction was monitoredvisually (refluxing and/or viscosity changes). For catalyst compositionscontaining an activator-support, the transition metal amine compound andthe activator-support were charged to a vial equipped with a stirbar.TIBA was added while stirring, followed by the α-olefin at the settemperature. For the reactions at elevated temperatures, the vial wasmaintained at the respective elevated temperature.

Table I summarizes certain reaction conditions, yields, and molecularweights (residual monomer was excluded) for Examples 9-24, whichemployed catalyst compositions containing either an aluminoxane or afluorinated organoboron compound. Generally, such catalyst compositionsalso containing TM-1, TM-2, or TM-3 (with alkyl or alkenyl groups on theN atom) required long reaction times and exhibited poor yields.Conversely, the catalyst compositions containing TM-A or TM-C (withheteroatom groups on the N atom) required a short reaction time andresulted in quantitative yield. Of the catalyst compositions containingTM-1, TM-2, or TM-3, those with the propenyl substituent on the N atomgenerally had the higher catalyst activity.

Table II summarizes certain reaction conditions, yields, and molecularweights (residual monomer was excluded) for Examples 25-45, whichemployed catalyst compositions containing an activator-support and anorganoaluminum compound. Unexpectedly, such catalyst compositions alsocontaining TM-1, TM-2, or TM-3 (with alkyl or alkenyl groups on the Natom) produced ultrahigh molecular weight polymers, with M_(w)'s inexcess of 1,000,000 g/mol, and generally at improved yields.Additionally, the catalyst compositions containing TM-A or TM-C (withheteroatom groups on the N atom) produced low molecular weight polymersover a wide range of reaction temperatures; M_(w)'s were in the 6,000 to21,000 range, significantly lower than the M_(w)'s produced using TM-Aor TM-C and either an aluminoxane or a fluorinated organoboron compound(see Table I) under analogous reaction conditions.

Table III summarizes certain reaction conditions, yields, and molecularweights (residual monomer was excluded) for Examples 37-39 and 46-53.Examples 37-39 and 46-51 employed catalyst compositions containing anactivator-support, an organoaluminum compound, and TM-1, TM-2, or TM-3(with alkyl or alkenyl groups on the N atom). Regardless of the α-olefinreactant—1-hexene, 1-octene, or 1-decene—an ultrahigh molecular weightpolymer unexpectedly was produced, most with M_(w)'s in excess of4,000,000 g/mol. FIG. 4 illustrates the molecular weight distributionsof the polymers of Examples 37-39. In Examples 52-53, a Ziegler-basedcatalyst system (commercially available as Lynx 200) was used, butresulted in polymers of much lower molecular weights when compared withthe polymers produced by catalyst compositions containing anactivator-support.

TABLE I Summary of Examples 9-24. Yield Reaction M_(w)/1000 ExampleCatalyst Composition α-olefin (%) Time (g/mol) 9 3 mg TM-A/10 mg[Ph₃C][B(C₆F₅)₄] 8 mL 1-hexene Quant.  5 min 163 10 3 mg TM-C/10 mg[Ph₃C][B(C₆F₅)₄] 8 mL 1-hexene Quant. 10 min 60 11 3 mg TM-C/6 mgB(C₆F₅)₃ 8 mL 1-hexene Quant. 30 min 125 12 3 mg TM-3/10 mg[Ph₃C][B(C₆F₅)₄] 8 mL 1-hexene 13 24 hr 1 13 3 mg TM-1/10 mg[Ph₃C][B(C₆F₅)₄] 8 mL 1-hexene 46 24 hr 2 14 3 mg TM-2/10 mg[Ph₃C][B(C₆F₅)₄] 8 mL 1-hexene <5 24 hr — 15 3 mg TM-A/300 mg ~20% MAOon Silica 8 mL 1-hexene Quant. 10 min 120 16 3 mg TM-C/300 mg ~20% MAOon Silica 8 mL 1-hexene Quant.  5 min 92 17 3 mg TM-A/300 mg ~20% MAO onSilica 8 mL 1-octene Quant. 10 min 139 18 3 mg TM-C/300 mg ~20% MAO onSilica 8 mL 1-octene Quant.  5 min 117 19 3 mg TM-3/300 mg ~20% MAO onSilica 8 mL 1-hexene <5 24 hr — 20 3 mg TM-1/300 mg ~20% MAO on Silica 8mL 1-hexene <5 24 hr — 21 3 mg TM-2/300 mg ~20% MAO on Silica 8 mL1-hexene <5 24 hr — 22 3 mg TM-3/0.5 mL 10% MAO in PhMe 6 mL 1-hexene <524 hr 6 23 3 mg TM-1/0.5 mL 10% MAO in PhMe 6 mL 1-hexene 31 24 hr 7 243 mg TM-2/0.5 mL 10% MAO in PhMe 6 mL 1-hexene <5 24 hr 10

TABLE II Summary of Examples 25-45. Yield Temperature ReactionM_(w)/1000 Example Catalyst Composition α-olefin (%) (° C.) Time (g/mol)25 3 mg TM-A/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 19 25 24 hr 7 26 3mg TM-C/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 93 25 24 hr 13 27 3 mgTM-A/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-hexene 85 25 24 hr 14 28 3 mgTM-C/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-hexene 96 25 24 hr 13 29 3 mgTM-A/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-hexene 70 25 24 hr 19 30 3 mgTM-C/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-hexene 96 25 24 hr 21 31 3 mgTM-C/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-octene 98 60 24 hr 10 32 3 mgTM-C/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-octene 98 60 24 hr 13 33 3 mgTM-C/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-octene 96 60 24 hr 20 34 3 mgTM-C/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-octene 91 90 24 hr 6 35 3 mgTM-C/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-octene 94 90 24 hr 10 36 3 mgTM-C/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-octene 89 90 24 hr 14 37 3 mgTM-3/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 81 25 24 hr 4,586 38 3 mgTM-1/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 19 25 24 hr 4,471 39 3 mgTM-2/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 41 25 24 hr 4,438 40 3 mgTM-3/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-hexene 91 25 24 hr 758 41 3 mgTM-1/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-hexene 69 25 24 hr 3,131 42 3 mgTM-2/0.1 g AS2/0.5 mL 1M TIBA 8 mL 1-hexene 6 25 24 hr 4,284 43 3 mgTM-3/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-hexene 13 25 24 hr 1,590 44 3 mgTM-1/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-hexene <5 25 24 hr 2,641 45 3 mgTM-2/0.1 g AS3/0.5 mL 1M TIBA 8 mL 1-hexene <5 25 24 hr 2,927

TABLE III Summary of Examples 37-39 and 46-53. Exam- Yield ReactionM_(w)/1000 ple Catalyst Composition α-olefin (%) Time (g/mol) 37 3 mgTM-3/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 81 24 hr 4,586 38 3 mgTM-1/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 19 24 hr 4,471 39 3 mgTM-2/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-hexene 41 24 hr 4,438 46 3 mgTM-3/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-octene 93 24 hr 4,237 47 3 mgTM-1/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-octene 28 24 hr 4,355 48 3 mgTM-2/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-octene 46 24 hr 4,253 49 3 mgTM-3/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-decene 83 24 hr 3,909 50 3 mgTM-1/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-decene 34 24 hr 4,579 51 3 mgTM-2/0.1 g AS1/0.5 mL 1M TIBA 8 mL 1-decene 47 24 hr 4,354 52 3 mg Lynx200/0.25 mL 1M TIBA 8 mL 1-hexene 93  3 hr 687 53 3 mg Lynx 200/0.25 mL1M TIBA 8 mL 1-decene 90 24 hr 1,736

The invention claimed is:
 1. A process for producing a product, theprocess comprising: contacting a catalyst composition and an alphaolefin monomer comprising a C₄ to C₆₀ alpha olefin to produce theproduct, the catalyst composition comprising: (i) anN,N-bis[2-hydroxidebenzyl]amine compound having formula (Ia):

wherein: M is Ti, Zr, or Hf; X¹ and X² independently are a monoanionicligand; each R^(B) and R^(C) independently is a halide, a C₁ to C₃₆hydrocarbyl group, a C₁ to C₃₆ halogenated hydrocarbyl group, a C₁ toC₃₆ hydrocarboxy group, or a C₁ to C₃₆ hydrocarbylsilyl group, wherein pand q independently are 0, 1, 2, 3, or 4; and R^(A) is a C₁ to C₃₆hydrocarbyl group or C₁ to C₃₆ halogenated hydrocarbyl group; (ii) anactivator-support comprising a solid oxide treated with anelectron-withdrawing anion; and (iii) optionally, a co-catalyst.
 2. Theprocess of claim 1, wherein R^(A) is a C₁ to C₁₂ hydrocarbyl group. 3.The process of claim 2, wherein: M is Zr or Hf; X¹ and X² independentlyare H, BH₄, a halide, a C₁ to C₃₆ hydrocarbyl group, a C₁ to C₃₆hydrocarboxy group, a C₁ to C₃₆ hydrocarbylaminyl group, a C₁ to C₃₆hydrocarbylsilyl group, a C₁ to C₃₆ hydrocarbylaminylsilyl group, OBR¹₂, or OSO₂R¹, wherein R¹ is a C₁ to C₃₆ hydrocarbyl group; and eachR^(B) and R^(C) independently is Cl, CF₃, a methyl group, an ethylgroup, a propyl group, a butyl group, a pentyl group, a hexyl group, aheptyl group, an octyl group, a nonyl group, a decyl group, an ethenylgroup, a propenyl group, a butenyl group, a pentenyl group, a hexenylgroup, a heptenyl group, an octenyl group, a nonenyl group, a decenylgroup, a phenyl group, a tolyl group, a benzyl group, a naphthyl group,a trimethylsilyl group, a triisopropylsilyl group, a triphenylsilylgroup, or an allyldimethylsilyl group.
 4. The process of claim 1,wherein the N,N-bis[2-hydroxidebenzyl]amine compound has formula (Ib):

wherein, in formula (Ib): M is Ti, Zr, or Hf; X¹ and X² independentlyare a monoanionic ligand; R^(B1), R^(B2), R^(C1), and R^(C2)independently are a halide, C₁ to C₃₆ hydrocarbyl group, C₁ to C₃₆halogenated hydrocarbyl group, C₁ to C₃₆ hydrocarboxy group, or C₁ toC₃₆ hydrocarbylsilyl group; and R^(A) is a C₁ to C₁₈ hydrocarbyl groupor C₁ to C₁₈ halogenated hydrocarbyl group.
 5. The process of claim 4,wherein: R^(B1), R^(B2), R^(C1), and R^(C2) independently are a methylgroup, ethyl group, propyl group, butyl group, pentyl group, hexylgroup, propenyl group, butenyl group, pentenyl group, hexenyl group,phenyl group, tolyl group, benzyl group, trimethylsilyl group,triisopropylsilyl group, triphenylsilyl group, allyldimethylsilyl group,CF₃, or Cl; and R^(A) is a methyl group, ethyl group, propyl group,butyl group, pentyl group, hexyl group, propenyl group, butenyl group,pentenyl group, hexenyl group, phenyl group, benzyl group, orphenylethyl group.
 6. The process of claim 1, wherein theN,N-bis[2-hydroxidebenzyl]amine compound is:

or a combination thereof.
 7. The process of claim 1, wherein thecatalyst composition comprises: an organoaluminum compound comprisingtrimethylaluminum, triethylaluminum, tri-n-propylaluminum,tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum,tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminumethoxide, diethylaluminum chloride, or any combination thereof; and anactivator-support comprising fluorided alumina, chlorided alumina,bromided alumina, sulfated alumina, fluorided silica-alumina, chloridedsilica-alumina, bromided silica-alumina, sulfated silica-alumina,fluorided silica-zirconia, chlorided silica-zirconia, bromidedsilica-zirconia, sulfated silica-zirconia, fluorided silica-titania,fluorided silica-coated alumina, sulfated silica-coated alumina,phosphated silica-coated alumina, or any combination thereof.
 8. Theprocess of claim 1, wherein the alpha olefin monomer comprises 1-hexene,1-octene, 1-decene, 1-tetradecene, or a mixture thereof.
 9. The processof claim 1, wherein the process is conducted at a temperature in a rangefrom −20° C. to 150° C.
 10. The process of claim 1, wherein the producthas a M_(w) of at least about 250,000 g/mol.
 11. The process of claim 1,wherein: X¹ and X² independently are a halide or a C₁ to C₁₈ hydrocarbylgroup; each R^(B) and R^(C) independently is a halide, a C₁ to C₁₈hydrocarbyl group, or a C₁ to C₁₈ hydrocarbylsilyl group, wherein p andq independently are 0, 1, or 2; R^(A) is a C₁ to C₁₈ hydrocarbyl group;the activator-support comprises a fluorided solid oxide, a sulfatedsolid oxide, or a combination thereof; and the alpha olefin monomercomprises a C₄ to C₂₀ alpha olefin.
 12. The process of claim 11,wherein: the catalyst composition comprises a co-catalyst; the processis conducted at a temperature in a range from 10° C. to 60° C.; and theproduct has a M_(w) in a range from 750,000 to 7,500,000 g/mol.
 13. Theprocess of claim 11, wherein: M is Zr or Hf; X¹ and X² independently area halide, methyl, benzyl, or phenyl; each R^(B) and R^(C) independentlyis a C₁ to C₅ alkyl group; and the alpha olefin monomer comprises a C₆to C₁₄ normal alpha olefin.
 14. The process of claim 13, wherein: R^(A)is a C₁ to C₈ alkyl group or a C₃ to C₈ terminal alkenyl group; thecatalyst composition comprises an organoaluminum co-catalyst; and thealpha olefin monomer comprises 1-hexene, 1-octene, 1-decene,1-tetradecene, or a mixture thereof.
 15. The process of claim 4, whereinthe catalyst composition comprises a co-catalyst, and wherein, informula (Ib): M is Zr or Hf; X¹ and X² independently are a halide or aC₁ to C₁₈ hydrocarbyl group; R^(B1), R^(B2), R^(C1), and R^(C2)independently are a halide, a C₁ to C₁₈ hydrocarbyl group, or a C₁ toC₁₈ hydrocarbylsilyl group; and R^(A) is a C₁ to C₁₈ hydrocarbyl group.16. The process of claim 15, wherein: the alpha olefin monomer comprisesa C₄ to C₂₀ alpha olefin; the activator-support comprises fluoridedalumina, chlorided alumina, bromided alumina, sulfated alumina,fluorided silica-alumina, chlorided silica-alumina, bromidedsilica-alumina, sulfated silica-alumina, fluorided silica-zirconia,chlorided silica-zirconia, bromided silica-zirconia, sulfatedsilica-zirconia, fluorided silica-titania, fluorided silica-coatedalumina, sulfated silica-coated alumina, phosphated silica-coatedalumina, or any combination thereof; and R^(B1), R^(B2), R^(C1), andR^(C2) independently are a C₁ to C₅ alkyl group.
 17. The process ofclaim 16, wherein: the alpha olefin monomer comprises a C₆ to C₁₄ normalalpha olefin; the product has a M_(w) in a range from 750,000 to7,500,000 g/mol; the activator-support comprises fluorided alumina,sulfated alumina, fluorided silica-alumina, sulfated silica-alumina,fluorided silica-coated alumina, sulfated silica-coated alumina, or anycombination thereof; the catalyst composition comprises anorganoaluminum co-catalyst; and in formula (Ib): X¹ and X² independentlyare a halide, methyl, benzyl, or phenyl; and R^(A) is a C₁ to C₈ alkylgroup or a C₃ to C₈ terminal alkenyl group.
 18. The process of claim 4,wherein: the alpha olefin monomer comprises a C₆ to C₁₄ normal alphaolefin; the catalyst composition comprises a co-catalyst; the process isconducted at a temperature in a range from −20° C. to 150° C.; and theproduct has a M_(w) in a range from 750,000 to 7,500,000 g/mol.
 19. Theprocess of claim 18, wherein, in formula (Ib): M is Zr or Hf; X¹ and X²independently are a halide or a C₁ to C₁₈ hydrocarbyl group; R^(B1),R^(B2), R^(C1), and R^(C2) independently are a halide, a C₁ to C₁₈hydrocarbyl group, or a C₁ to C₁₈ hydrocarbylsilyl group; and R^(A) is aC₁ to C₁₈ hydrocarbyl group.
 20. The process of claim 19, wherein: thecatalyst composition comprises an organoaluminum co-catalyst; theactivator-support comprises a fluorided solid oxide, a sulfated solidoxide, or a combination thereof; the process is conducted at atemperature in a range from 10° C. to 60° C.; the alpha olefin monomercomprises 1-hexene, 1-octene, 1-decene, 1-tetradecene, or a mixturethereof; and in formula (Ib): X¹ and X² independently are a halide,methyl, benzyl, or phenyl; R^(B1), R^(B2), R^(C1), and R^(C2)independently are a C₁ to C₅ alkyl group; and R^(A) is a C₁ to C₈ alkylgroup or a C₃ to C₈ terminal alkenyl group.